Nitrogen-containing carbon alloy, process of producing the same, and carbon catalyst containing the same

ABSTRACT

A nitrogen-containing carbon alloy obtained by baking an organic material having a nitrogen-containing crystalline organic compound having a molecular weight of 60 to 2000, wherein the nitrogen-containing crystalline organic compound excludes a nitrogen-containing metal complex.

CROSS-REFERENCE TO RELATED APPLICATION(S)

The present application claims priority from Japanese Patent ApplicationNo. 2010-079924 filed on Mar. 30, 2010, the entire content of which isincorporated herein by reference.

BACKGROUND

1. Field

This invention relates to a nitrogen-containing carbon alloy, a processof producing the carbon alloy, and a carbon catalyst containing thecarbon alloy. More particularly, it relates to an N-containing carbonalloy obtained from a low-molecular N-containing crystalline organiccompound, a process of producing the same, and a carbon catalystcontaining the same.

2. Description of the Related Art

Catalysts based on noble metals, such as platinum and palladium, havebeen applied for their high oxygen reduction activity to, for example,solid polyelectrolyte fuel cells used in automobiles, and domestic powerand heat supply systems. However, the noble metal-based catalysts aretoo costly to be used even more widely.

Research and development have therefore been invested into platinum-freecatalysts or catalysts with greatly reduced use of platinum. Forexample, JP 2007-26746A proposes a catalyst having carbon alloy obtainedby baking a polymer resulting from polymerization of a mixture of aprecursor of a resin, such as polyfurfuryl alcohol, phenol formaldehydeor melamine resin, and a metal complex, such as cobalt phthalocyanine oriron phthalocyanine. Such a carbon alloy catalyst is known to have highoxygen reduction activity because it is obtained by uniformly dispersingthe metal complex in a resin precursor followed by decomposing otherthan the metal, for example, phthalocyanine moiety so that the metal isuniformly distributed in the catalyst as reported in “Proceedings of the'09 Meeting and Workshop of Fuel Cell-Related Catalyst Division inCatalyst Society of Japan”.

JP 2009-173627A describes an electrode catalyst for fuel cells which isobtained by heating a mixture of a metal complex and an organic cycliccompound. JP 2009-234918A discloses a catalyst having a modified metalcomplex obtained by subjecting a mononuclear-metal complex having anaromatic skeleton to a modification treatment selected from a heattreatment, an irradiation treatment with a radiation, and a dischargetreatment.

The problem of these processes is that the polymer material containslow-molecular impurities, such as a solvent, and needs removal of theimpurities, which makes the production process complicated. In contrast,processes starting with a low molecular compound are advantageous inthat the low molecular compound may previously be purified to provide ahigh purity precursor. This offers a broader choice of precursormaterials.

Carbon alloys prepared from low molecular compounds include thoseobtained by baking a metal complex and an unsaturated compound asdisclosed in JP 2009-39623A and those obtained by baking a metal complexand a polycyclic organic compound having at least two hetero atoms onthe same ring as disclosed in JP 2010-270107A. However, metal complexesare difficult to purify, and the unsaturated compound is structurallylimited because it must react with the ligand of the metal complex. Dueto these problems it is not easy to stably prepare a carbon alloy ofhigh oxygen reduction activity, and the advantage of using a lowmolecular compound is hardly achieved. “Jun Murayama, Carbon, 48, 3271(2010)” reports preparation of a carbon alloy by baking a mixture of anitrogen-containing polycyclic organic compound, ferric gluconate, andmagnesium acetate, but the oxygen reduction activity of this carbonalloy catalyst is lower than that of the carbon alloys of polymer originso that it is difficult to eliminate the need to use a noble metal suchas platinum or palladium.

On the other hand, metal-free low molecular compounds are free of theproblems, such as difficulty of purification and structural limitation.Using a metal-free low molecular compound, nevertheless, poses thefollowing problem. “Jun Murayama and Ikuo Abe, Journal of theElectrochemical Society, 154(3), B297 (2007)”, for example, reports acase in which a mixture of an amino acid, glucose, and iron lactate isdehydrated and baked. The report reveals that the amino acid alonedecomposes at 350° C. and cannot carbonize, indicating the difficulty incarbonizing a metal-free low molecular compound by baking. It has thusbeen believed by those skilled in the art that a carbon alloy is notobtained from a metal-free low molecular compound.

SUMMARY

An object of the invention is to provide a carbon alloy which has ametal other than noble metals uniformly supported therein and therebyexhibits sufficiently high oxygen reduction activity and which isobtained by baking a low-molecular organic compound that is easy topurify and may have a wide choice of structure; a process of producingthe carbon alloy; and a carbon catalyst containing the carbon alloy.

As a result of extensive investigation, the inventors of the presentinvention have found that an N-containing carbon alloy with sufficientlyhigh oxygen reduction activity is obtainable by baking an organicmaterial having an N-containing crystalline organic compound with amolecular weight of 60 to 2000. They have also found that, when aninorganic metal or an inorganic metal salt is admixed with theN-containing crystalline organic compound, there is obtained anN-containing carbon alloy having the metal uniformly supported thereinand exhibiting further increased oxygen reduction activity. Theinvention has thus been completed based on these findings.

Although a metal-free low molecular compound vaporizes on baking,vaporization of the compound on baking is suppressed by crystallizingthe compound to impart increased intermolecular action. By the use ofthe crystallized compound, carbon alloys having various interstitialstructures corresponding to the crystal structure of the crystallizedcompound can easily be prepared, which allows for controlling thecatalyst activity or electric conductivity that is closely related tothe interstitial structure.

There is a report that it is desirable to remove a metal oxide and thelike from organic materials (see JP-2009-234918). To the contrary, theinventors have ascertained that better effects are obtained when inusing an organic material containing at least one of an inorganic metaland an inorganic metal salt. It is considered that, when an N-containingcrystalline low molecular compound and an inorganic metal or aninorganic metal salt are used in combination, the metal atoms andnitrogen atoms, which are positioned along the crystal edges with greatregularity and uniformity to exert mutual action with each otherpreviously and, as a result, a catalytically-competent nitrogen to metalratio is achieved spontaneously to provide a carbon alloy having highoxygen reduction activity.

The above objects of the invention are accomplwashed by the provision ofthe following subject matter.

<1> A nitrogen-containing carbon alloy obtained by baking an organicmaterial having a nitrogen-containing crystalline organic compoundhaving a molecular weight of 60 to 2000, wherein the nitrogen-containingcrystalline organic compound excludes a nitrogen-containing metalcomplex.<2> The nitrogen-containing carbon alloy according to <1>, wherein theorganic material further has at least one of an inorganic metal and aninorganic metal salt.<3> The nitrogen-containing carbon alloy according to <1>, wherein thenitrogen-containing crystalline organic compound is a nitrile compound,an amide compound or a quinacridone compound.<4> The nitrogen-containing carbon alloy according to <1>, wherein thenitrogen-containing crystalline organic compound has at least one groupselected from the group consisting of a nitrile group, an amido groupand 4-quinolone structure, and an unsaturated bond per molecule.<5> The nitrogen-containing carbon alloy according to <4>, wherein thenitrogen-containing crystalline organic compound has at least oneselected from the group consisting of a nitrile group and an amidogroup, at least one selected from the group consisting of a nitrilegroup, an amido group, a halogen atom, and a hydroxyl group, and anunsaturated bond per molecule.<6> The nitrogen-containing carbon alloy according to <1>, wherein thenitrogen-containing crystalline organic compound is a pigment.<7> The nitrogen-containing carbon alloy according to <1>, wherein thenitrogen-containing crystalline organic compound has a nitrogen contentof 0.1% to 55% by mass.<8> The nitrogen-containing carbon alloy according to <1>, wherein theorganic material is a volatile-retardant compound having a ΔTG value of−95% to −0.1% at 400° C. in a nitrogen atmosphere.<9> The nitrogen-containing carbon alloy according to <1>, wherein thebaking is carried out at a baking temperature of 500° to 1000° C. in astream of inert gas or non-oxidizing gas.<10> The nitrogen-containing carbon alloy according to <9>, wherein theinert gas or non-oxidizing gas flows at a flow rate of 0.01 to 2.0 l/minper 36 mm inner diameter.<11> A process for producing the nitrogen-containing carbon alloyaccording to <2>, having: mixing the nitrogen-containing crystallineorganic compound and the at least one of the inorganic metal and theinorganic metal salt; raising a temperature of the mixture from roomtemperature to a carbonization temperature of the mixture in an inertatmosphere at a rate of 1° C./min to 1000° C./min; maintaining themixture at a temperature of 500° to 1000° C. for 0.1 to 100 hours toachieve carbonization; and cooling the carbonized mixture from thecarbonization temperature to room temperature.<12> A carbon catalyst having the nitrogen-containing carbon alloyaccording to <1>.<13> A fuel cell having the carbon catalyst according to <12> and apolyelectrolyte.<14> An electrical storage device having the carbon catalyst accordingto <12>.

According to the invention, an N-containing carbon alloy havingsufficiently high oxygen reduction activity is obtained by baking anorganic material containing a low molecular crystalline N-containingorganic compound that is easy to purify and may have a wide choice ofstructure. When an inorganic metal or an inorganic metal salt is admixedwith the crystalline N-containing organic compound, there is obtained anN-containing carbon alloy having the metal uniformly supported therein,exhibiting further increased oxygen reduction activity, and having adesired lattice structure. The N-containing carbon alloy is useful as acarbon catalyst. The carbon catalyst is applicable to fuel cells andenvironmental catalysts. The invention also provides a process forproducing the N-containing carbon alloy.

BRIEF DESCRIPTION OF DRAWINGS

FIG. 1 schematically illustrates a fuel cell having a carbon alloy ofthe invention.

FIG. 2 schematically illustrates an electrical double-layer capacitorhaving a carbon alloy of the invention.

FIG. 3 graphically represents voltage-current density curves of the fuelcells of Examples 2, 4, 5, 8, 10, 14, 21, and 24 and Comparative Example4.

DETAILED DESCRIPTION OF INVENTION

The term “Hammett constant op” that will be used in the followingdescription is briefly explained below. The Hammett's rule is anempirical rule proposed by L. P. Hammett in 1935 in an attempt toquantitatively discuss the influences of a substituent of a benzenederivative on the reaction or equilibrium, the validity of which is nowgenerally admitted. Substituent constants obtained by the Hammett's ruleinclude σp and σm values. These values are found in many general books,for example, J. A. Dean (ed.), Lange's Handbook of Chemistry, the 12thEd., MacGraw-Hill (1979) and Kagakuno Ryoiki, Extra Ed., No. 122, pp.96-103, Nankodo (1979). In the following description, varioussubstituents will be limited or described in terms of Hammett constantsσp. This does not mean that intended substituents are limited to thosesubstituents the σp value of which is known from literature, andintended substituents include any substituent of which the σp value isnot found in literature but seems to fall within a recited range whendetermined based on Hammett's rule. While the pigments represented byformulae (1) and (2) that will be described later for use in theinvention are not benzene derivatives, the electronic effect of theirsubstituent will be represented by the measure σp irrespective of theposition of the substituent. Note that the σp values will be used inthat sense hereinafter.

As used herein, the term “substituent” means any atom or group ofatomics capable of substitution. Examples of the substituent includehalogen atoms (e.g., fluorine, chlorine, bromine, and iodine), ahydroxyl group, a cyano group, aliphatic groups (e.g., aralkyl,cycloalkyl, and active methine), an aryl group (which may be bonded atany position thereof), a heterocyclic group (which may be bonded at anyposition thereof), an acyl group, aliphatic oxy groups (e.g., alkoxy,alkyleneoxy, or a group having repeated ethyleneoxy or propyleneoxyunits), an aryloxy group, a heterocyclic oxy group, an aliphaticcarbonyl group, an arylcarbonyl group, a heterocyclic carbonyl group, analiphatic oxycarbonyl group, an aryloxycarbonyl group, a heterocyclicoxycarbonyl group, a carbamoyl group, a sulfonylcarbamoyl group, anacylcarbamoyl group, a sulfamoylcarbamoyl group, a thiocarbamoyl group,an aliphatic carbonyloxy group, an aryloxycarbonyloxy group, aheterocyclic carbonyloxy group, an amino group, an aliphatic aminogroup, an arylamino group, a heterocyclic amino group, an acylaminogroup, an aliphatic oxyamino group, an aryloxyamino group, asulfamoylamino group, an acylsulfamoylamino group, an oxamoylaminogroup, an aliphatic oxycarbonylamino group, an aryloxycarbonylaminogroup, a heterocyclic oxycarbonylamino group, a carbamoylamino group, amercapto group, an aliphatic thio group, an arylthio group, aheterocyclic thio group, an alkylsulfinyl group, an arylsulfinyl group,an aliphatic sulfonyl group, an arylsulfonyl group, a heterocyclicsulfonyl group, an aliphatic sulfonylureido group, an arylsulfonylureidogroup, a heterocyclic sulfonylureido group, an aliphatic sulfonyloxygroup, an arylsulfonyloxy group, a heterocyclic sulfonyloxy group, asulfamoyl group, an aliphatic sulfamoyl group, an arylsulfamoyl group, aheterocyclic sulfamoyl group, an acylsulfamoyl group, asulfonylsulfamoyl group or a salt thereof, a carbamoylsulfamoyl group, asulfonamido group, an aliphatic ureido group, an arylureido group, aheterocyclic ureido group, an aliphatic sulfonamido group, anarylsulfonamido group, a heterocyclic sulfonamido group, an aliphaticsulfinyl group, an arylsulfinyl group, a nitro group, a nitroso group, adiazo group, an azo group, a hydrazino group, a di-aliphaticoxyphosphinyl group, a diaryloxyphosphinyl group, silyl groups (e.g.,trimethylsilyl, t-butyldimethylsilyl, and phenyldimethylsilyl), silyloxygroups (e.g., trimethylsilyloxy and t-butyldimethylsilyloxy), a boronogroup, and ionic hydrophilic groups (e.g., carboxyl, sulfo, phosphono,and quaternary ammonium group). These substituents may further have asubstituent selected, for example, from the substituents recited above.

(I) N-Containing Carbon Alloy

The N-containing carbon alloy of the invention is obtained by baking anorganic material containing an N-containing crystalline organic compoundhaving a molecular weight of 60 to 2000.

[Nitrogen-Containing Crystalline Organic Compound]

As used herein, the term “N-containing crystalline organic compound”means a compound having crystallinity and containing nitrogen andincludes hydrocarbon compounds with a carbon atom of the hydrocarbonstructure replaced with a hetero atom, such as oxygen, nitrogen, orsulfur, and hydrocarbon compounds with a hydrogen atom of thehydrocarbon structure replaced with a functional group containing ahetero atom, such as oxygen, nitrogen, or sulfur. The N-containingcrystalline organic compound should have crystallinity so that themolecules of the compound may be regularly oriented with ease. It shouldbe noted, however, that N-containing metal complexes are excluded fromthe N-containing crystalline organic compound because, for one thing,they are difficult to purify and, for another, the N-containing ligandto metal complex ratio is fixed so that, when they decompose on baking,the decomposition rate of the N-containing ligand and the vaporizationrate of the coordinated metal complex cannot be controlled, presentingdifficulties in obtaining an intended N-containing carbon alloy. Evenwhen an N-containing metal complex and a low molecular organic compoundare mixed, the N-containing metal complex crystals decompose, and themetal is directly subjected to reduction. As a result, neighboring metalatoms thus produced are liable to agglomerate and crystallize. Becausethe metal is removed by acid cleaning, the resulting N-containing carbonalloy is non-uniform only to have reduced functionality. For use as, forexample, a catalyst, the resulting N-containing carbon alloy will havereduced catalyst activity. For these reasons, N-containing metalcomplexes are not suited for use in the invention.

[Crystal Structure]

The N-containing crystalline organic compound that can be used in theinvention is selected with considerations given to π-π interaction,coordinate bond, charge transfer interaction, and hydrogen bond. It ispreferred that the N-containing crystalline organic compound have acrystal structure formed by at least two bonds or interactions. By theuse of a low molecular compound having such a crystal structure, theintermolecular interaction is enhanced, thereby allowing for control onvaporization during baking in the preparation of an N-containing carbonalloy.

As used herein, the term “crystal structure” refers to the arrangementor alignment of molecules within a crystal. In other words, a crystalstructure is composed of repeated unit cells. Molecules are located atany position and oriented in the unit cell and oriented. Moleculesassume uniform conformation in a crystal. That is, because thefunctional group is uniformly arranged in a crystal, the intermolecularinteraction is equal in and out of the unit cell. In the case of, forinstance, an N-containing crystalline organic compound having a stackingstructure, an interaction is exerted between aromatic rings,heterocyclic rings, fused polycyclic structures, fused polyheterocyclicstructures, or unsaturated groups (e.g., C≡N, vinyl, allyl, oracetylene). For example, aromatic rings arranged face to face exert π-πinteraction (often referred to as π-π stacking) The molecules pile up atregular interval by the intermolecular overlapping of the sp2 or sporbitals of carbon atoms of unsaturated bond in these rings or groupsthereby to form stacked columnar assemblies.

The columnar assemblies have a uniform structure, in which adjacentcolumns are arranged with a specific intermolecular distance by hydrogenbonds or van der Waals forces. This is advantageous in that heattransfer within crystals is easily accomplished.

The N-containing crystalline organic compound used in the invention is alow molecular compound and yet has crystallinity and exhibits heatresistance due to vibration relaxation by phonons (quantized latticevibration). Therefore, the decomposition temperature is maintained tothe carbonization temperature so that carbonization is accomplished withreduced vaporization of decomposition products to form a carbon alloystructure.

A noncrystalline compound is unfavorable because molecular orientationis uncontrollable during baking only to provide a non-uniform structuralcarbon material.

It is preferred that the N-containing crystalline organic compound havea melting temperature of 25° C. or higher. If the melting temperature islower than 25° C., there will not be an air layer during baking, whichcontributes to heat resistance, and the compound will boil or bump basedon the temperature vs. vapor pressure relation, resulting in a failureto obtain a carbon material.

The N-containing crystalline organic compound for used in the inventionis not particularly limited as long as it is a crystalline organiccompound containing a nitrogen atom and having a molecular weight of 60to 2000. The molecular weight of the N-containing crystalline organiccompound is preferably 100 to 1500, more preferably 130 to 1000.

The N-containing crystalline organic compound preferably has at leastone functional group selected from, for example, the above mentionedgroup of substituents and/or a heterocyclic group. In particular, theN-containing crystalline organic compound preferably has at least onefunctional group selected from halogen (e.g., chlorine, chlorine,bromine, or iodine), hydroxyl, cyano, aliphatic carbonyl, arylcarbonyl,heterocyclic carbonyl, aliphatic oxycarbonyl, aryloxycarbonyl,heterocyclic oxycarbonyl, aliphatic amino, arylamino, heterocyclicamino, acylamino, aliphatic oxyamino, aryloxyamino, sulfamoylamino,acylsulfamoylamino, oxamoylamino, aliphatic oxycarbonylamino,aryloxycarbonylamino, heterocyclic oxycarbonylamino, and carbamoylamino.Examples of the N-containing crystalline organic compound includeamines, imines, nitriles, imides, and amides. Nitrile compounds, amidecompounds and quinacridone compounds are preferred in terms ofcrystallinity and heat resistance, and nitrile compounds and amidecompounds are more preferred.

The N-containing crystalline organic compound is preferably an organiccompound having an unsaturated bond and at least one group selected fromthe group consisting of a nitrile group, an amido group and 4-quinolonestructure in the molecule thereof, more preferably an organic compoundhaving at least one group selected from a nitrile group and an amidogroup and an unsaturated bond in the molecule thereof, further morepreferably an organic compound having at least one group selected from anitrile group and an amido group, at least one group selected from anitrile group, an amido group, a halogen atom, and a hydroxyl group, andan unsaturated bond in the molecule thereof, still further morepreferably an organic compound having at least one group selected from anitrile group and an amido group, at least one group selected from anitrile group, an amido group, and a halogen atom, and an unsaturatedbond in the molecule thereof.

It is believed that starting with an N-containing crystalline organiccompound having a nitrile group or an amido group in its moleculeresults on baking in the formation of active sites composed of C, N, andmetal atoms having high oxygen reduction activity in the resultingN-containing carbon alloy.

It is preferred for the N-containing crystalline organic compound tohave an aromatic ring formed by unsaturated bonds. The aromatic ring ispreferably a heterocyclic ring having one hetero atom or a benzene ring,with a substituted or unsubstituted benzene ring and a substituted orunsubstituted pyridine ring being particularly preferred. The presenceof the unsaturated bonds is considered to induce the above describedinteraction to form a carbon alloy skeleton.

When the molecules of the N-containing crystalline organic compoundhave, for example, nitrogen (N) of an amido, amine, or nitrile group, ahetero atom of a hetero ring (e.g., N of a pyridyl group), a chalcogenelement (e.g., O, S, or Se) of a carbonyl, ether, or hydroxyl group), ora halogen element (e.g., F, Cl, Br, or I) between adjacent stackedcolumns, these atoms form hydrogen bonds with protons (H⁺). Thus, theassembly of the stacked columns may be controlled by at least oneinteraction, such as hydrogen bonds, coordinate bonds, charge transferinteraction, acid-base interaction, and van der Waals interaction, or bymultiple interaction exerted two-dimensionally or three-dimensionally inthe network.

The N-containing crystalline organic compounds may be used eitherindividually or as a mixture of two or more thereof. The N-containingcrystalline organic compound preferably has a metal content of not morethan 10 ppm. The N-containing crystalline organic compound with theabove recited molecular weight is easy to purify before baking.

The nitrogen content of the N-containing crystalline organic compound ispreferably 0.1% to 55%, more preferably 1% to 30%, even more preferably4% to 20%, by mass. When in using the N-containing crystalline organiccompound with the nitrogen content in that range, there is no need toseparately introduce a nitrogen-containing compound as a nitrogensource, and nitrogen atoms and metal atoms are regularly and uniformlyarranged along the crystal edges and allowed to show interaction witheach other easily. As a result, a nitrogen to metal ratio exhibitinghigher oxygen reduction activity will be obtained.

The N-containing crystalline organic compound is preferably avolatile-retardant compound having a ΔTG value of −95% to −0.1%, morepreferably −95% to −1%, even more preferably −90% to −5%, at 400° C. ina nitrogen atmosphere. As will be described in detail, the N-containingcrystalline organic compound may be mixed with an inorganic metal or aninorganic metal salt as long as the N-containing crystalline organiccompound is capable of carbonization without vaporization during baking.

The term “ΔTG” or “ΔTG value” as used herein denotes a percent mass lossof the organic material, i.e., the N-containing crystalline organiccompound or a mixture of the N-containing crystalline organic compoundand an inorganic metal or inorganic metal salt, at 400° C. relative tothe mass at room temperature (30° C.) measured by TG-DTA analysis inwhich the compound or the mixture is heated from 30° C. to 1000° C. at arate of temperature rise of 10° C./min, under flowing nitrogen. Thevolatile-retardant N-containing crystalline organic compound having theΔTG value falling within the range recited is prevented from decomposingduring baking, which affords an increased carbon yield.

The N-containing heterocyclic compounds include N-containingheterocyclic monocyclic compounds and N-containing fused heterocycliccompounds. Suitable N-containing heterocyclic monocyclic compoundsinclude 5-membered ring compounds, such as pyrrole and its derivatives,diazole compounds (e.g., pyrazole and imidazole) and their derivatives,and triazole compounds and their derivatives; and 6-membered ringcompounds, such as pyridine and its derivatives, diazine compounds(e.g., pyridazine, pyrimidine, and pyrazine) and their derivatives, andtriazine compounds and their derivatives (e.g., melamine or cyanuricacid). Suitable N-containing fused heterocyclic compounds includequinoline, phenanthroline, and purine.

Examples of the amines include primary, secondary, and tertiary amines,diamines, triamines, polyamines, and amino compounds. The primary totertiary amines include aliphatic amines, such as methylamine,ethylamine, dimethylamine, and trimethylamine, and aromatic amines(e.g., aniline) and derivatives thereof. The diamines are exemplified byethylenediamine. The amino compounds include amino alcohols exemplifiedby ethanolamine. Examples of the imines include pyrrolidine andethyleneimine. Examples of the nitriles include aliphatic nitriles, suchas acetonitrile; aromatic nitriles and halides thereof, such asbenzonitrile, phthalonitrile, isophthalonitrile, terephthalonitrile, andtetracyanobenzene; isonitrile; and amino acids. Examples of the amidesinclude carboxylic acid amides, N-substituted amides, (N-mono- anddisubstituted amides), aromatic amides (aromatic mono- and diamides),urea, carbamide, urethane, lactam, lactim, hydrazide, imidic acid, andimidic esters.

The N-containing heterocyclic compound is preferably a pigment. Pigmentsform uniform stacked columnar assemblies via intermolecular π-πinteraction, with the adjacent columns arranged with a specificintermolecular distance by hydrogen bonds or van der Waals forces.Therefore, heat transfer within crystals is easily accomplished.Although the pigments are low molecular compounds, they havecrystallinity and exhibit heat resistance due to vibration relaxation byphonons (quantized lattice vibration). Therefore, the decompositiontemperature is maintained to the carbonization temperature so thatcarbonization is accomplished with reduced vaporization of decompositionproducts.

Preferred pigments are isoindoline pigments, isoindolinone pigments,diketopyrrolopyrrole pigments, quinacridone pigments, oxazine pigments,phthalocyanine pigments, quinophthalone pigments, latent pigmentsderived from the above described pigments (described hereinafter), andlake pigments obtained by combining dyes with a metal ion, withdiketopyrrolopyrrole pigments, quinacridone pigments, isoindolinepigments, isoindolinone pigments, quinophthalone pigments, latentpigments derived from these pigments being more preferred. On baking,the pigment decomposes to form a benzonitrile (Ph-CN) structure, whichacts as a reaction active species to provide a carbon alloy catalystwith higher oxygen reduction reaction (ORR) activity. When a metalspecies (M) is present in the system, the pigment forms a Ph-CN . . . Mcomplex on baking to provide a carbon alloy with still higher ORRactivity.

The N-containing crystalline organic compounds include a compoundrepresented by formula (1) shown below, a tautomer thereof, or a salt ora hydrate of the compound of formula (1) and the tautomer.

In the formula (1), each of Z₁ and Z₂ independently represents ahydrogen atom, an aliphatic group, an aryl group, a heterocyclic group,an acyl group, a hydroxyl group, an aliphatic oxycarbonyl group, acarbamoyl group (—CONH₂), or a sulfonyl group; n represents an integer 1to 3; when n=2, the compound is a dimer formed via Z₁ and Z₂, and whenn=3, the compound is a trimer formed via a benzene or triazine ringcontaining Z₁ and Z₂; and A represents any one of the following formulae(A-1) to (A-39).

In the formulae (A-1) to (A-39), each of R₅₁, R₅₂, R₅₃, R₅₄, R₅₅, R₅₆,R₅₇, R₅₈, R₅₉, and R₆₀ independently represent hydrogen or asubstituent; adjacent substituents may be connected to each other toform a 5- or 6-membered ring; and the asterisk mark * indicates theposition of the bond to the pyrrolidone structures.

The aliphatic group as represented by Z₁ and Z₂ may be substituted orunsubstituted and saturated or unsaturated. The substituent thealiphatic group may have may be any one of those which are listed aboveand able to substitute for hydrogen of the aliphatic group. Thealiphatic group is preferably an alkyl group having 1 to 8 carbon atoms,more preferably alkyl having 1 to 6 carbon atoms, e.g., methyl, ethyl,isopropyl, cyclohexyl, or t-butyl.

The aryl group as represented by Z₁ and Z₂ may be optionallysubstituted. The substituent the aryl group may have may be any one ofthose which are listed above and able to substitute for hydrogen on thearyl group. The aryl group is preferably an aryl group having 6 to 12carbon atoms, more preferably an aryl group having 6 to 10 carbon atoms,such as phenyl, 3-methoxyphenyl, or 4-carbamoylphenyl.

The heterocyclic group as represented by Z₁ and Z₂ may be optionallysubstituted, saturated or unsaturated, and monocyclic or a fused ringsystem. The substituent the heterocyclic group may have may be any oneof those which are listed above and able to substitute for hydrogen ofthe heterocyclic group. The heterocyclic group is preferably aheterocyclic group having 2 to 16 carbon atoms, more preferably a 5- or6-membered heterocyclic group having 2 to 12 carbon atoms, such as1-pyrrolidinyl, 4-morpholinyl, 2-pyridyl, 1-pyrrolyl, 1-imidazolyl, or1-benzimidazolyl.

The aliphatic oxycarbonyl group as represented by Z₁ and Z₂ may beoptionally substituted and saturated or unsaturated. The substituent thealiphatic oxycarbonyl group may have may be any one of those which arelisted above and able to substitute for hydrogen of the aliphaticoxycarbonyl group. The aliphatic oxycarbonyl group is preferably analkoxycarbonyl group having 1 to 8 carbon atoms, more preferably analkoxycarbonyl group having 1 to 6 carbon atoms, such asmethoxycarbonyl, ethoxycarbonyl, isopropoxycarbonyl, orcarbamoylmethoxycarbonyl.

The carbamoyl group as represented by Z₁ and Z₂ may be optionallysubstituted. The substituent the carbamoyl group may have may be any oneof those which are listed above and able to substitute for hydrogen ofthe carbamoyl group and is preferably an aliphatic group, an aryl group,or a heterocyclic group. The optionally substituted carbamoyl group ispreferably a carbamoyl group, an alkylcarbamoyl group having 2 to 9carbon atoms, a dialkylcarbamoyl group having 3 to 10 carbon atoms, anarylcarbamoyl group having 7 to 13 carbon atoms, or a heterocycliccarbamoyl group having 3 to 12 carbon atoms, more preferably a carbamoylgroup, an alkylcarbamoyl group having 2 to 7 carbon atoms, adialkylcarbamoyl group having 3 to 6 carbon atoms, an arylcarbamoylgroup having 7 to 11 carbon atoms, or a heterocyclic carbamoyl grouphaving 3 to 10 carbon atoms, such as carbamoyl, methylcarbamoyl,dimethylcarbamoyl, phenylcarbamoyl, or 4-pyridinecarbamoyl.

The sulfamoyl group as represented by Z₁ and Z₂ may be substituted orunsubstituted. The substituent the sulfamoyl group may have may be anyone of those which are listed above and able to substitute for hydrogenof the sulfamoyl group and is preferably an aliphatic group, an arylgroup, or a heterocyclic group. The optionally substituted sulfamoylgroup is preferably a sulfamoyl group, an alkylsulfamoyl group having 1to 9 carbon atoms, a dialkylsulfamoyl group having 2 to 10 carbon atoms,an arylsulfamoyl group having 7 to 13 carbon atoms, or a heterocyclicsulfamoyl group having 2 to 12 carbon atoms, more preferably a sulfamoylgroup, an alkylsulfamoyl group having 1 to 7 carbon atoms, adialkylsulfamoyl group having 3 to 6 carbon atoms, an arylsulfamoylgroup having 6 to 11 carbon atoms, or a heterocyclic sulfamoyl grouphaving 2 to 10 carbon atoms, such as sulfamoyl, methylsulfamoyl,N,N-dimethylsulfamoyl, phenylsulfamoyl, or 4-pyridinesulfamoyl.

Z₁ and Z₂ may be connected to each other to form a 5- or 6-memberedring. Examples of the ring formed by Z₁ and Z₂ include benzene,pyridine, pyrazine, pyrimidine, triazine, pyridazine, pyrrole, pyrazole,imidazole, triazole, oxazole, oxadiazole, thiazole, thiadiazole, furan,thiophene, selenophene, silole, germole, phosphole, and pyrrolidonerings, with pyrrolidone, benzene, pyridine, pyrazine, pyrimidine,triazine, pyridazine, pyrrole, pyrazole, imidazole, and triazole ringsbeing preferred, and with a pyrrolidone ring being more preferred.

The substituent as R₅₁ to R₆₀ may be any of those listed above and ableto substitute for hydrogen as R₅₁ to R₆₀. Suitable substituents as R₅₁to R₅₉ are halogen (e.g., fluorine, chlorine, bromine, or iodine),aliphatic, aryl, heterocyclic, hydroxyl, acyl, aliphatic oxycarbonyl,optionally substituted carbamoyl, acylamino, sulfonamido, aliphatic oxy,aliphatic thio, cyano, or sulfonyl, preferably halogen (e.g., fluorine,chlorine, bromine, or iodine), aliphatic, aryl, heterocyclic, hydroxyl,aliphatic oxycarbonyl, optionally substituted carbamoyl, optionallysubstituted ureido, aliphatic oxy, or cyano.

From the viewpoint of effects of the invention, each of R₅₁ to R₅₉ ispreferably hydrogen, halogen (e.g., fluorine, chlorine, bromine, oriodine), aliphatic, aryl, heterocyclic, hydroxyl, acyl, aliphaticoxycarbonyl, optionally substituted carbamoyl, optionally substitutedureido, acylamino, sulfonamido, aliphatic oxy, aliphatic thio, cyano, orsulfonyl, more preferably hydrogen, halogen (e.g., fluorine, chlorine,bromine, or iodine), aliphatic, aliphatic oxycarbonyl, optionallysubstituted carbamoyl, optionally substituted ureido, aliphatic oxy, orcyano.

The substituent as R₆₀ may be any of those listed above and able tosubstitute for hydrogen as R₆₀. Preferred substituents as R₆₀ are analiphatic group, an aryl group, a heterocyclic group, and an aromatic 5-or 6-membered heterocyclic ring formed through R₆₀ and the substituentR₅₁ to R₅₉ adjacent to R₆₀, with an aliphatic group, an aryl group, a 5-or 6-membered aromatic heterocyclic group having nitrogen at an orthoposition relative to the position of the bond, and an aromatic 5- or6-membered heterocyclic ring formed through R₆₀ and the substituent R₅₁to R₅₉ adjacent to R₆₀ being more preferred.

In terms of the effects of the invention, R₆₀ is preferably an aliphaticgroup, an aryl group, or a heterocyclic group, more preferably analiphatic group, an aryl group, a 5- or 6-membered aromatic heterocyclicgroup having nitrogen at an ortho position relative to the position ofthe bond, or an aromatic 5- or 6-membered heterocyclic ring formedthrough R₆₀ and the substituent R₅₁ to R₅₉ adjacent to R₆₀, even morepreferably a 5- or 6-membered aromatic heterocyclic group havingnitrogen at an ortho position relative to the position of the bond or anaromatic 5- or 6-membered heterocyclic ring formed through R₆₀ and thesubstituent R₅₁ to R₅₉ adjacent to R₆₀. When R₆₀ is a 5- or 6-memberedaromatic heterocyclic group having nitrogen at an ortho positionrelative to the position of the bond, not only intermolecular π-πinteraction but intramolecular interaction by hydrogen bonding areexerted to readily impart heat resistance. When an aromatic 5- or6-membered heterocyclic ring formed through R₆₀ and the substituent R₅₁to R₅₉ adjacent to R₆₀ is included, not only heat resistance is impartedby the intermolecular π-π interaction, but also nitrogen doping intographene of carbon alloy is easily achieved, thereby to provideexcellent ORR activity.

The substituents as R₅₂, R₅₃, and R₅₄ may be any one of those listedabove and able to substitute for hydrogen on the ring. In terms of theeffects of the invention, each of R₅₂ to R₅₄ is preferably aheterocyclic group or an electron withdrawing group having a Hammettconstant σp of 0.20 or greater, more preferably an electron withdrawinggroup having a Hammett constant σp of 0.30 or greater. The upper limitof the σp value is 1.0.

Examples of the electron withdrawing group with a σp value of 0.20 orgreater as R₅₂ to R₅₄ are an acyl group, an acyloxy group, a carbamoylgroup, an alkyloxycarbonyl group, an aryloxycarbonyl group, a cyanogroup, a nitro group, a dialkylphosphono group, a diarylphosphono group,a diarylphosphinyl group, an alkylsulfinyl group, an arylsulfinyl group,an alkylsulfonyl group, an arylsulfonyl group, a sulfonyloxy group, anacylthio group, a sulfamoyl group, a thiocyanate group, a thiocarbonylgroup, a haloalkyl group, a haloalkoxy group, a haloaryloxy group, ahaloalkylamino group, a haloalkylthio group, an aryl substituted withanother electron withdrawing group having a σp value of 0.20 or greater,a heterocyclic group, a halogen group, an azo group, and a selenocyanategroup.

In the formula (1), A is preferably any one of (A-1) to (A-16) and(A-39), more preferably any one of (A-1) to (A-4), (A-6) to (A-8),(A-10), and (A-39).

On decomposing the compound of formula (1), a CN bond is formed in thedecomposition product because of the cyclic structure (A-1) to (A-39).The CN bond and a metal interact with each other, whereby nitrogen isretained until carbonization. As a result, nitrogen is easily introducedinto the graphene layers of carbon alloy to impart excellent ORRactivity. In particular, it is preferred to use a pigment having such astructural characteristic.

Of the heterocyclic structures (A-2) to (A-39), the N-containingstructures (A-2) to (A-4), (A-6) to (A-8), (A-10), and (A-39) arepreferred because nitrogen atoms in the hetero ring will regularly alignalong crystal edges originating from the N-containing crystallineorganic compound to allow free metal ions to coordinate therewith.

The N-containing crystalline organic compound of the formula (1) ispreferably represented by formula (2).

In the formula (2), each of Z₁ and Z₂ independently represent a hydrogenatom, an aliphatic group, an aryl group, a heterocyclic group, an acylgroup, a hydroxyl group, an aliphatic oxycarbonyl group, a carbamoylgroup (—CONH₂), or a sulfonyl group; n represents an integer 1 to 3;when n=2, the compound is a C2 symmetric dimer formed via Z₁ and Z₂, andwhen n=3, the compound is a C3 symmetric trimer formed via a benzenering containing Z₁ and Z₂.

The preferred types and scopes of Z₁, Z₂, A, and n in formula (2) arethe same as in formula (1).

The N-containing crystalline organic compound of the formula (2) ispreferably represented by formula (3).

In the formula (3), A represents any one of (A-1) to (A-39). Theasterisk mark * indicates the position of the bond to A in the formula(3).

The preferred types and scopes of A in the formula (3) are the same asin the formula (1).

The N-containing crystalline organic compound of the formula (1) ispreferably represented by the formula (4).

In the formula (4), each of Z₁ and Z₂ independently represents ahydrogen atom, an aliphatic group, an aryl group, a heterocyclic group,an acyl group, a hydroxyl group, an aliphatic oxycarbonyl group, acarbamoyl group (—CONH₂), or a sulfonyl group; n represents an integer 1to 3; when n=2, the compound is a C2 symmetric dimer formed via Z₁ andZ₂, and when n=3, the compound is a C3 symmetric trimer formed via abenzene ring containing Z₁ and Z₂; and R₆₁, R₆₂, R₆₃, R₆₄, and R₆₅ eachrepresent a hydrogen atom or a substituent; and adjacent substituentsmay be connected to each other to form a 5- or 6-membered ring.

The preferred types and scopes of R₆₁ to R₆₅ are the same as those ofR₅₁ to R₅₅ in formula (1).

The N-containing crystalline organic compound of the formula (3) or (4)is preferably represented by formula (5).

In the formula (5), each of R₆₁, R₆₂, R₆₃, R₆₄, R₆₅/R₆₆, R₆₇, R₆₈, R₆₉,and R₇₀ independently represents a hydrogen atom or a substituent, andadjacent two of the substituents R₆₁ to R₇₀ may be connected to eachother to form a 5- or 6-membered ring.

The preferred types and scopes of R₆₁ to R₇₀ in the formula (5) are thesame as those of R₅₁ to R₅₅ in the formula (1).

The specific examples of the compound represented by the formula (1) areshown below, but the invention is not restricted to these compounds.

In the following specific examples, Me stands for a methyl group, Bustands for a butyl group, and Ph stands for a phenyl group.

The pigment that can be used in the invention is not structurallylimited and may be any of magenta, yellow, and cyan pigments. Suitableorganic pigments include perylene pigments, perynone pigments,quinacridone pigments, quinacridonequinone pigments, anthraquinonepigments, anthanthrone pigments, benzimidazolone pigments, disazocondensation pigments, disazo pigments, azo pigments, indanthronepigments, indanthrene pigments, quinophthalone pigments,quinoxalinedione pigments, metal-free phthalocyanine pigments,triarylcarbonium pigments, dioxazine pigments, aminoanthraquinonepigments, diketopyrrolopyrrole pigments, naphthol AS pigments,thioindigo pigments, isoindoline pigments, isoindolinone pigments,pyranthrone pigments, isobioranthrone pigments, mixtures of thesepigments, latent pigments derived from these pigments, mixtures of thelatent pigments, and mixtures of the latent pigments and the abovedescribed pigments.

Examples of suitable pigments include perylene pigments, such as C.I.Pigment Red 190 (PR190, C.I. No. 71140), C.I. Pigment Red 224 (PR224,C.I. No. 71127), and C.I. Pigment Violet 29 (PV29, C.I. No. 71129);perynone pigments, such as C.I. Pigment Orange 43 (PO43, C.I. No. 71105)and C.I. Pigment Red 194 (PR 194, C.I. No. 71100); quinacridonepigments, such as C.I. Pigment Violet 19 (PV19, C.I. No. 73900), C.I.Pigment Violet 42 (PV42), C.I. Pigment Red 122 (PR122, C.I. No. 73915),C.I. Pigment Red 192 (PR192, C.I. No. 739155), C.I. Pigment Red 202(PR202, C.I. No. 73907), C.I. Pigment Red 207 (PR207, C.I. No. 73900,73906), and C.I. Pigment Red 209 (PR209, C.I. No. 73905);quinacridonequinone pigments, such as C.I. Pigment Red 206 (PR206, C.I.No. 73900/73920), C.I. Pigment Orange 48 (PO48, C.I. No. 73900/73920),and C.I. Pigment Orange 49 (PO49, C.I. No. 73900/73920); anthraquinonepigments, such as C.I. Pigment yellow 147 (PY147, C.I. No. 60645);anthanthrone pigments, such as C.I. Pigment Red 168 (PR168, C.I. No.59300); benzimidazolone pigments, such as C.I. Pigment Brown 25 (PB25,C.I. No. 12510), C.I. Pigment Violet 32 (PV32, C.I. No. 12517), C.I.Pigment Yellow 180 (PY180, C.I. No. 21290), C.I. Pigment yellow 181(PY181, C.I. No. 11777), C.I. Pigment Orange 62 (PO62, C.I. No. 11775),and C.I. Pigment Red 185 (PR185, C.I. No. 12516); disazo condensationpigments, such as C.I. Pigment Yellow 93 (PY93, C.I. No. 20710), C.I.Pigment yellow 94 (PY94, C.I. No. 20038), C.I. Pigment Yellow 95 (PY95,C.I. No. 20034), C.I. Pigment yellow 128 (PY128, C.I. No. 20037), C.I.Pigment Yellow 166 (PY166, C.I. No. 20035), C.I. Pigment Orange 34(PO34, C.I. No. 21115), C.I. Pigment Orange 13 (P013, C.I. No. 21110),C.I. Pigment Orange 31 (PO31, C.I. No. 20050), C.I. Pigment Red 144(PR144, C.I. No. 20735), C.I. Pigment Red 166 (PR166, C.I. No. 20730),C.I. Pigment Red 220 (PR220, C.I. No. 20055), C.I. Pigment Red 221(PR221, C.I. No. 20065), C.I. Pigment Red 242 (PR242, C.I. No. 20067),C.I. Pigment Red 248 (PR248), C.I. Pigment Red 262 (PR262), and C.I.Pigment Brown 23 (PB23, C.I. No. 20060); disazo pigments, such as C.I.Pigment yellow 13 (PY13, C.I. No. 21100), C.I. Pigment Yellow 83 (PY83,C.I. No. 21108), and C.I. Pigment Yellow 188 (PY188, C.I. No. 21094);azo pigments, such as C.I. Pigment Red 187 (PR187, C.I. No. 12486), C.I.Pigment Red 170 (PR170, C.I. No. 12475), and C.I. Pigment Yellow 74(PY74, C.I. No. 11714); indanthrone pigments, such as C.I. Pigment Blue60 (PB60, C.I. No. 69800); quinophthalone pigments, such as C.I. PigmentYellow 138 (PY138, C.I. No. 56300); phthalocyanine pigments, such asC.I. Pigment Green 7 (PG7, C.I. No. 74260), C.I. Pigment Green 36 (PG36,C.I. No. 74265), and Pigment Blue 16 (PB16, C.I. No. 74100); dioxazinepigments, such as C.I. Pigment Violet 23 (PV23, C.I. No. 51319) and C.I.Pigment Violet 37 (PV37, C.I. No. 51345); aminoanthraquinone pigments,such as C.I. Pigment Red 177 (PR177, C.I. No. 65300);diketopyrrolopyrrole pigments, such as C.I. Pigment Red 254 (PR254, C.I.No. 56110), C.I. Pigment Red 255 (PR255, C.I. No. 561050), C.I. PigmentRed 264 (PR264, C.I. No. 561300), C.I. Pigment Red 272 (PR272, C.I. No.561150), C.I. Pigment Orange 71 (P071, C.I. No. 561200), and C.I.Pigment Orange 73 (P073); thioindigo pigments, such as C.I. Pigment Red88 (PR88, C.I. No. 73312); isoindoline pigments, such as C.I. PigmentYellow 139 (PY139, C.I. No. 56298), C.I. Pigment Yellow 185 (PY185, C.I.No. 12516), C.I. Pigment Orange 66 (PO66, C.I. No. 48210), and C.I.Pigment Orange 69 (PO69, C.I. No. 56292); isoindolinone pigments, suchas C.I. Pigment Yellow 109 (PY109, C.I. No. 56284), C.I. Pigment Yellow110 (PY110, C.I. No. 56280), C.I. Pigment Yellow 137 (PY137, C.I. No.561600), and C.I. Pigment Orange 61 (PO61, C.I. No. 11295); pyranthronepigments, such as C.I. Pigment Orange 40 (PO40, C.I. No. 59700) and C.I.Pigment Red 216 (PO216, C.I. No. 59710); and isobioranthrone pigments,such as C.I. Pigment Violet 31 (PV31, C.I. No. 60010). Preferred of themare quinacridone pigments, diketopyrrolopyrrole pigments, isoindolinepigments, quinophthalone pigments, and latent pigments derived fromthese pigments. Particularly preferred pigments are diketopyrrolopyrrolepigments, such as C.I. Pigment Red 254 (PR54, C.I. No. 56110), C.I.Pigment Red 255 (PR255, C.I. No. 561050), C.I. Pigment Red 264 (PR264,C.I. No. 561300), C.I. Pigment Red 272 (PR272, C.I. No. 561150), C.I.Pigment Orange 71 (P071, C.I. No. 561200), and C.I. Pigment Orange 73(P073); quinacridone pigments, such as C.I. Pigment Violet 19 (PV19,C.I. No. 73900), C.I. Pigment Violet 42 (PC42), C.I. Pigment Red 122(PR122, C.I. No. 73915), C.I. Pigment Red 192 (PR192, C.I. No. 739155),C.I. Pigment Red 202 (PR202, C.I. No. 73907), C.I. Pigment Red 207(PR207, C.I. No. 73900, 73906), and C.I. Pigment Red 209 (PR209, C.I.No. 73905); isoindoline pigments, such as C.I. Pigment Yellow 139(PY139, C.I. No. 56298), C.I. Pigment Yellow 185 (PY185, C.I. No.12516), C.I. Pigment Orange 66 (PO66, C.I. No. 48210), C.I. PigmentOrange 69 (PO69, C.I. No. 56292); isoindolinone pigments, such as C.I.Pigment Yellow 109 (PY109, C.I. No. 56284), C.I. Pigment Yellow 110(PY110, C.I. No. 56280), C.I. Pigment Yellow 137 (PY137, C.I. No.561600), and C.I. Pigment Orange 61 (PO61, C.I. No. 11295); andquinophthalone pigments, such as C.I. Pigment Yellow 138 (PY138, C.I.No. 56300).

Latent pigments derived from the above described pigments are alsouseful. The latent pigments may be used individually or as a mixture oftwo or more thereof or in combination with the pigments.

As used herein, the term “latent pigment” is intended to mean a compoundhaving a thermally decomposable group and capable of being easilyconverted to an organic pigment by applying energy such as heat. Thelatent pigment is exemplified by a pigment compound having introduced tothe pigment base thereof a protective group enhancing solventsolubility. The protective group is easily released by, for example,chemical, photolytic, or thermal treatment, whereby the latent pigmentis converted to an insoluble pigment having its essential color. For thedetails of latent pigments, reference may be made to Nature, vol. 388,p. 131 (1997). Examples of suitable latent pigments with various colorsand structures are given, e.g., in JP 9-3362A, WO 98/32802, WO 98/45757,WO 98/58027, WO 99/01511, JP 11-92695A, and JP 11-310726A.

Latent pigments that are preferably used in the invention are compounddescribed in the paragraph [0066] and [Chemical formulae 21 to 27] in JP2010-83982A. Commercially available latent pigments may be used as well.Particularly preferred latent pigments are PR 254-LP and PR 122-LP shownbelow.

The N-containing crystalline organic compounds also include a compoundrepresented by formula (11) shown below, a tautomer thereof, or a saltor a hydrate of the compound of the formula (11) and the tautomer.

N

A  (11)

In the formula (11), A represents any one of the formulae (A-1) to(A-39), in which adjacent two of the substituents R₅₁ to R₆₀ may beconnected to each other to from a 5- or 6-membered ring or aheterocyclic fused ring system, and the asterisk mark * indicates theposition of the bond to the nitrile structure in the formula (11).

Preferred types and scopes of the substituents in the cyclic structures(A-1) to (A-39) are the same as for those in the formula (1).

Of the compounds of the formula (11), preferred are those represented byformulae (13) to (18). In the following specific examples, Ph representsa phenyl group, t-Bu represents a tert-butyl group.

[Inorganic Metal and Inorganic Metal Salt]

The organic material preferably contains at least one member selectedfrom an inorganic metal and an inorganic metal salt in addition to theN-containing crystalline organic compound. In this preferred embodiment,there can be obtained a carbon alloy exhibiting higher oxygen reductionactivity by the interaction between nitrogen and metal atoms. That is,the N-containing crystalline organic compound decomposes on baking, andthe decomposition product forms an N-containing carbon alloy catalyst ina vapor phase. When metal exists in the vapor phase, the decompositionproduct interacts with the metal to form a complex. The resultingN-containing carbon alloy catalyst thus shows improved activity.

The carbon alloy takes the form of fine carbon particles at least partof which preferably have a turbostratic structure, such as a nanoshellstructure.

It is more preferred that the carbon alloy of the present embodimentcontains a transition metal or a transition metal compound. In the morepreferred embodiment, the carbon alloy is produced by carbonizing theN-containing crystalline organic compound, which contains nitrogen atoms(N) as a constituent element. It is preferred that, on baking theN-containing crystalline organic compound, the nitrogen atoms beimmobilized on the surface of the carbon alloy at high concentration bythe catalytic action of the transition metal or transition metalcompound added to the N-containing crystalline organic compound, therebyforming carbon particles having the nitrogen atoms and the transitionmetal or transition metal compound mutually acting on each other.

The carbon alloy of the present embodiment exhibits high activitypresumably for the following reason. The N-containing crystallineorganic compound has a uniform structure in which molecules are stackedinto columnar structures by the intermolecular pi-pi interaction, andthe adjacent columns are arranged with a specific intermoleculardistance by hydrogen bonds or van der Waals forces. The N-containingcrystalline organic compound decomposes and/or vaporizes on heating.Because of being uniform and crystalline, the compound exhibitsexcellent heat transfer. As a result, a high concentration of reactionsites is provided, and carbon crystals form at many points. In somecases, interaction occurs with the transition metal or transition metalcompound to catalytically promote carbonization. Therefore, a basicstructure of a carbon alloy is generally a stack of graphene layers madeof sp2-bonded carbon atoms packed in a two-dimensionally extendinghoneycomb lattice.

The carbon alloy of the present embodiment is considered to becharacterized by extremely large number of edge planes.

The N-containing crystalline organic compound is not particularlylimited in shape as long as the carbon catalyst activity will be shown.For example, it may be spherical or have a largely distorted shape, suchas elliptic, flattened, or angular. The form of the N-containingcrystalline organic compound may be sheet-like, fibrous, columnar, orparticulate.

The metal of at least one of the inorganic metal and the inorganic metalsalt is not particularly limited as long as the carbon catalyst activityis not hindered. Usable metals include di- to tetra-valent typicalmetals, transition metals, and inner transition metals. Examples of thetypical metals are Al, Si, Ga, Ge, As, In, Sn, Sb, Tl, and Pb. Examplesof the transition metals include Sc, Ti, V, Cr, Mn, Fe, Co, Ni, Cu, Zn,Y, Zr, Nb, Mo, Tc, Ru, Rh, Pd, Ag, Cd, La, Hf, Ta, W, Re, Os, Ir, Pt,Au, and Hg. Examples of the inner transition metals include lanthanidesand actinides, e.g., Ce, Pr, Nd, Pm, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb,Lu, Th, Pa, U, Np, and Am.

Preferred of them are transition metals, particularly those belonging tothe fourth period of Groups 3 to 12 of the Periodic Table, such as Co,Fe, Mn, Ni, Cu, Ti, V, Cr, Zn, Zr, Nb, Mo, Ta, and Ce, with Co, Fe, Mn,Ni, Cr, Cu, and Ce being especially preferred. Co, Fe, Mn) Ni, Cr, Cu,and Ce, and compounds thereof (such as salts thereof) are competent toform a nanoshell structure that improves the carbon catalyst activity.Of them, Co and Fe are particularly superior in forming a nanoshellstructure. Furthermore, Co or Fe incorporated into the carbon catalystis able to enhance the oxygen reduction activity of the carbon alloycatalyst. The most preferred transition metal is Co because aCo-containing N-containing carbon alloy is superior in storage stabilityowing to its non-susceptibility to functional deterioration due tooxidation with time.

The carbon alloy may contain one or more element(s) other than thetransition metals, such as boron, alkali metals (e.g., Na, K, and Cs),alkaline earth metals (e.g., Mg, Ca, and Ba), Pb, Sn, In, and Tl.

The inorganic metal salts include, but are not limited to, hydroxides,oxides, nitrides, sulfates, sulfites, sulfides, sulfonates,carbonylates, nitrates, nitrites, and halides, with those having, as acounter ion, a halide ion, a nitrate ion, or a sulfate ion beingpreferred. The metal halide, nitrate, or sulfate having a halide,nitrate, or sulfate counter ion easily allows the metal element to bondto the surface carbon appearing on thermal decomposition to increase thespecific surface area.

The inorganic metal salt may contain crystallization water. The presenceof crystallization water of the inorganic metal salt provides improvedthermal conductivity, allowing for uniform baking. Examples of suitableinorganic metal salts containing crystallization water are cobaltchloride hydrates, iron (III) chloride hydrates, and iron (II) chloridehydrates.

The N-containing carbon alloy of the invention is preferably obtained bybaking an organic material containing 55 to 99.999 parts by mass of theN-containing crystalline organic compound and 0.001 to 45 parts by massof at least one of an inorganic metal and an inorganic metal salt, morepreferably an organic material containing 60 to 99.9 parts by mass ofthe N-containing crystalline organic compound and 0.1 to 40 parts bymass of at least one of an inorganic metal, and an inorganic metal salt,even more preferably an organic material containing 70 to 99 parts bymass of the N-containing crystalline organic compound and 1 to 30 partsby mass of at least one of an inorganic metal, and an inorganic metalsalt, each per 100 parts by mass of the total of the N-containingcrystalline organic compound and the inorganic metal and/or theinorganic metal salt.

The organic material having the above described preferred compositionprovides a carbon alloy with high ORR activity. When the content of theN-containing crystalline organic compound in the organic material isless than 55 parts, there are some cases in which metal atoms vaporizedfrom an inorganic metal or an inorganic salt gather to form clusters,which further congregate into metal particles. This is because the ratioof the N-containing crystalline organic compound to the inorganic metalor inorganic metal salt is so small that the inorganic metal orinorganic metal salt are not liable to interact with the decompositionproduct of the N-containing crystalline organic compound.

Metal particles of single nanometer size partly contribute to the ORRactivity whereas those exceeding several tens of nanometer take no partin the ORR activity.

While, at this time, the mechanism of the ORR activity is not entirelyclear, the following assumption can be made. The organic material formscatalytically active sites (metal coordination sites or spaces formed ofor by at least C, N, and a metal ion) on carbonization, so that oxygenis adsorbed by and coordinated to the active sites of the catalyst andthen reduced.

If large metal particles are formed in the step of baking, theprecipitated metal particles will be removed by acid cleaning aftergrinding. That is, catalytically active sites (metal coordination sitesor spaces), by and to which oxygen is to be adsorbed and coordinated,are not formed, resulting in a failure to exhibit sufficient ORRactivity.

On the other hand, when a metal source and the N-containing crystallineorganic compound are mixed in a ratio within the recited range, asufficient amount of the N-containing crystalline organic compoundexists around the individual metal species to prevent the metal atomsfrom associating into clusters. Therefore, an N-containing carbon alloyforms on baking the N-containing crystalline organic compound, and themetal mildly coordinates to the N-containing carbon alloy along theedges (where activity will develop) generated both inside and outsidethe resulting graphite to form catalytically active sites. TheN-containing carbon alloy thus exercises its ORR activity sufficiently.

The ORR activity may be represented by current density measured by themethod described in Examples hereinafter given. To attain a high output,the current density during oxygen reduction is preferably as loispossible. Specifically, the current density is preferably −100 μA/cm² orless, more preferably −300 μA/cm² or less, even more preferably −1100μA/cm².

The present embodiment is advantageous in that there is no need touniformly disperse the N-containing crystalline organic compound and theinorganic metal or inorganic metal salt in the preparation of theorganic material to be baked. The mixed state of the N-containingcrystalline organic compound and the inorganic metal or inorganic metalsalt at room temperature is not influential on the ORR activity of theresulting carbon alloy because what is necessary to form active specieshaving ORR activity is believed to be that the decomposition product ofthe N-containing crystalline organic compound and vapor of the inorganicmetal salt, etc. should be in contact with each other during baking.

The inorganic metal or inorganic metal salt preferably has a diameter of0.001 to 100 μm, more preferably 0.01 to 10 μm. The metallic particleswithin that size range are able to be uniformly admixed with theN-containing crystalline organic compound so that the N-containingcrystalline organic compound may easily form a complex on decomposition.The inorganic metal particles may have the surface thereof oxidized solong as an inorganic metal is reproduced during baking.

The following combinations are exemplified as preferred embodiments ofthe present invention.

Preferred combinations of the metal of at least one of the inorganicmetal and the inorganic metal salt and the N-containing crystallineorganic compound include a combination of iron, cobalt, iron salt, orcobalt salt and a nitrile compound, an amide compound, or a quinacridonecompound. A more preferred combination is cobalt, or cobalt salt and anorganic compound having at least one of a nitrile group, an amido group,and 4-quinolone structure and an unsaturated bond per molecule. An evenmore preferred combination is cobalt and an organic compound having atleast one of a nitrile group and an amido group, at least one of anitrile group, an amido group, a halogen atom, and a hydroxyl group andan unsaturated bond in the molecule thereof.

[Carbon Alloy]

The carbon alloy of the invention, which is obtained by baking the abovedescribed organic material, is an N-containing carbon alloy havingnitrogen doped therein. The carbon alloy of the invention has a stack ofgraphene layers made of sp2-bonded carbon atoms packed in atwo-dimensional honeycomb lattice. The carbon alloys having nitrogenatoms doped into the honeycomb lattice are divided according to thebinding form of nitrogen atom into the following types (i) through (iv).

(i) Oxide type (N_(OX)): A nitrogen atom binding to halogen, oxygen, andso on in an oxidized state.(ii) Graphitic type (N_(Q)): A nitrogen atom substituting for one of thecarbon atoms on the boundary between adjacent hexagons of a graphenelayer.(iii) Pyrrolic type (N₅): A nitrogen atom present in an N-containingpentagon, a result of change from a hexagon of a graphene layer.(iv) Pyridinic type (N₆): A nitrogen atom substituting for one carbonatom that is not on the border between adjacent hexagons of a graphenelayer, the carbon atom mostly being on the edge periphery of a graphenelayer(v) Pyridonic type (N₆*): A nitrogen atom binding to two carbon atoms tomake a hexagon, with one of the carbon atoms having OH or O bondedthereto.

The surface nitrogen content and the surface carbon content of thecarbon catalyst are determined by X-ray photoelectron spectroscopy(XPS). The N_(IS) XPS spectrum shows peaks at different binding energiesassigned to the difference of the above defined types of nitrogen atoms.With this feature taken advantage of, the peaks are separated to comparethe intensities, thereby to obtain the N to C ratio. Typical positionsof the peaks of the nitrogen atoms of the types described are shownbelow.

(i) N_(OX): 402.9±0.2 eV (ii) N_(Q): 401.2±0.2 eV

(iii) N₅: 400.5±0.2 eV

(iv) N₆: 398.5±0.2 eV

As stated, there can be pyridonic nitrogen (N₆*) atoms binding to carbonatoms having an OH group. However, N₆* nitrogen is not distinguishablefrom pyrrolic nitrogen (N₅) because it has an intensity peak at the samebinding energy as that of pyrrolic nitrogen (N₅)(400.5±0.2 eV) (see E.Raymundo-Pinero et al., Carbon, vol. 40, pp. 597-608 (2002)). Therefore,in the description of the invention, N₆* nitrogen atoms are described asbeing included in “N₅ nitrogen atoms”. Suitability of a nitrogen atomfor binding to metal is dependent on whether the nitrogen atom has anisolated electron pair. A nitrogen atom having an isolated electron pairdonates the electron pair to the unoccupied orbital of a metal ion toform a coordinate bond. Of the nitrogen atom types discussed above, N₅and N₆ nitrogen atoms having an isolated electron pair are effective inbinding to metal, whereas the N_(OX) and N_(Q) nitrogen atoms are noteffective. Accordingly, the ratio of the sum of the number of N₅nitrogen atoms and the number of N₆ nitrogen atoms to the total numberof nitrogen atoms as obtained by peak separation of the N_(1s) XPSspectrum, {(N₅+N₆)/N}, is preferably 0.2 to 1.0, more preferably 0.3 to1.0. When {(N₅+N₆)/N} is smaller than 0.2, the number of nitrogen atomscapable of binding to metal may be insufficient, which can result in afailure to obtain sufficient oxygen reduction catalytic characteristics.The upper limit of {(N₅+N₆)/N} is, in principle, 1.

It is more preferred that the carbon alloy catalyst have a surfacenitrogen content to surface carbon content ratio, N/C, of 0.05 to 0.3.When the N to C atomic ratio, N/C, is less than 0.05, the number ofnitrogen atoms capable of binding to metal may be insufficient, whichcan result in a failure to obtain sufficient oxygen reduction catalyzingcharacteristics. When the N/C exceeds 0.3, the carbon skeleton of thecarbon alloy has reduced strength and reduced electrical conductivity.

The carbon alloy should be composed of at least carbon atoms andnitrogen atoms and may contain other atoms, such as hydrogen and oxygen.In the latter case, the atomic ratio of the other atoms to the sum ofcarbon atoms and nitrogen atoms, other atoms/(C+N), is preferably 0.3 orsmaller.

The specific surface area of the carbon alloy may be determined by theBET method as follows. A carbon alloy sample is put in a prescribedcontainer and cooled to the liquid nitrogen temperature (−196° C.).Nitrogen gas is introduced into the container to be adsorbed by thecarbon alloy. An adsorption isotherm is prepared, from which amonomolecular adsorption and an adsorption parameter are calculated. Thespecific surface area of the sample is obtained from the results and theknown molecular area of nitrogen (0.162 cm²).

The specific surface area, average pore size, and pore volume of thecarbon alloy may be determined by the following procedures. A carbonalloy sample is put in a prescribed container and cooled to the liquidnitrogen temperature (−196° C.). Nitrogen gas is introduced into thecontainer, and the adsorbed nitrogen quantity is obtained by avolumetric method or a gravimetric method. The pressure of nitrogen gasintroduced is gradually increased, and the adsorbed gas quantity isplotted against each equilibrium pressure to obtain a nitrogenadsorption isotherm. The specific surface area, average pore size, andpore volume are calculated using the adsorption isotherm in accordancewith the subtracting pore effect (SPE) method (K. Kaneko, et al.,Carbon, 30, 1075 (1986)). The SPE method is a method to calculatespecific surface area and others by performing micropore analysis withthe use of the α_(s)-plot method, the t-plot method or the like andeliminating the effect of strong potential field of micropores. The SPEmethod achieves higher accuracy than the BET method in calculating thespecific surface area and the like of a macroporous sample.

The pore geometry of the carbon alloy is not particularly limited. Thepores may be only on the surface or not only on the surface but alsoinside of the carbon alloy. In the latter case, the carbon alloy mayhave pores passing through the carbon alloy like tunnels or may havespherical or polyhedral (e.g., hexagonal columnar) voids connected toeach other.

The specific surface area of the carbon alloy is preferably 30 m²/g ormore, more preferably 35 m²/g or more, even more preferably 40 m²/g ormore. When the specific surface area is less than 30 m²/g, the areacapable of being in contact with a substance to be supported and thenumber of pores capable of containing the substance are reduced,thereby, it may be insufficient to exhibit sufficient oxygen reductioncatalytic characteristics. When the carbon alloy has catalyticallyactive sites (metal coordination sites or spaces formed of or by atleast C, N, and a metal ion) at a high density, the specific surfacearea may be less than 30 m²/g. It should be noted that, with a specificsurface area of 1000 m²/g or more, oxygen may fail to reach the deepestpart of the pores, which can result in insufficient oxygen reductioncatalytic characteristics.

The average pore size of the carbon alloy is preferably 1 to 50 mu, morepreferably 2 to 10 nm. When the average pore size is smaller than 1 nm,the pores are often smaller than a component to be supported, which canresult in a failure to obtain sufficient ORR catalytic characteristics.When the average pore size is greater than 50 nm, the specific surfacearea tends to be insufficient to exhibit sufficient ORR catalyticcharacteristics.

The pore volume of the carbon alloy is not particularly limited; for itvaries with the specific surface area and the average pore size.Usually, the pore volume is preferably 0.1 to 50 ml/g, more preferably0.2 to 2.5 ml/g.

The form and shape of the carbon alloy are not particularly limited aslong as ORR activity is exhibited. The carbon alloy may be sheet-like,fibrous, block-like, columar, or particulate and may have a sphericalshape or a largely distorted shape, such as elliptic, flattened, orangular. Block-like or particulate forms are preferred in terms ofdispersibility.

The carbon alloy of the invention may be dispersed in a solvent(disperse medium) to make a slurry. The slurry may be applied to asubstrate, baked, and dried to make a carbon catalyst of desired shape.By the use of the slurry, a carbon catalyst is produced with improvedprocessability, which facilitates making an electrode catalyst of fuelcells or an electrode material of electrical storage devices.

The solvent is chosen appropriately from those commonly employed in theproduction of electrode catalysts of fuel cells or electrode materialsof electrical storage devices. In producing electrode materials ofelectrical storage devices, ordinary polar solvents, such as diethylcarbonate (DCE), dimethyl carbonate (DMC), 1,2-dimethoxyethane (DME),ethylene carbonate (EC), ethylmethyl carbonate (EMC),N-methyl-2-pyrrolidone (NMP), propylene carbonate (PC), and γ-lactone(GBL), are used either individually or as a mixture of two or morethereof. Examples of the solvents used in producing the electrodecatalyst of fuel cells include water, methanol, ethanol, isopropylalcohol, butanol, toluene, xylene, methyl ethyl ketone, and acetone.

In Raman spectrum analysis of the carbon alloy of the invention, thefull width at half maximum of the Raman G-band is preferably 60 cm⁻¹ ormore, more preferably 70 cm⁻¹ or more, even more preferably 80 cm⁻¹ ormore. The carbon alloy showing such a Raman spectrum has increased edgeson its surface to exhibit improved catalyst activity and shows equalcatalyst activity at any part of it.

(2) Process of Producing N-Containing Carbon Alloy

The process for producing the N-containing carbon alloy of the inventionincludes the steps of (1) mixing an N-containing crystalline organiccompound and an inorganic metal and/or an inorganic metal salt, (2)raising the temperature of the mixture from room temperature to acarbonization temperature in an inert atmosphere at a rate of 1° C./minto 1000° C./min, (3) maintaining the mixture at a temperature of 500° to1000° C. for 0.1 to 100 hours, and (4) cooling the mixture from thecarbonization temperature to room temperature.

The process of the invention is characterized by the step of heating anorganic material containing an N-containing crystalline organic compoundand an inorganic metal and/or an inorganic metal salt σp to acarbonization temperature.

In the step of heating σp to the carbonization temperature, the part ofthe heating operation in which the temperature is being raised is takenas an infusibilization treatment.

The baking temperature for carbonization is not so critical as long asthe N-containing crystalline organic compound undergoes pyrolysis andcarbonization at the temperature. It is preferably 500° to 1000° C.,more preferably 550° to 950° C., even more preferably 600° to 900° C. Atreaction temperatures of 500° C. or higher, carbonization proceedssufficiently to provide a carbon alloy with high catalyst performance.At reaction temperatures of 1000° C. or lower, nitrogen remains in theresulting carbon skeleton to give a desired N to C atomic ratio securingsufficient ORR activity. At reaction temperature exceeding 1000° C.,nitrogen hardly remains in the carbon skeleton, tending to result in areduced atomic N/C and reduced ORR activity. Furthermore, the yield ofthe carbonization product can considerably decrease.

Carbonization is achieved by maintaining the organic material at 500° to1000° C. for 0.1 to 100 hours, preferably 1 to 10 hours. Extending thecarbonizing time over 10 hours tends to result in a failure to obtainmerited effects.

Carbonization is preferably carried out in an inert atmosphere, forexample in a stream of inert gas or non-oxidizing gas. The gas flow rateis preferably 0.01 to 2.0 more preferably 0.05 to 1.0 l/min, even morepreferably 0.1 to 0.5 l/min, per 36 mm inner diameter. When the flowrate is less than 0.01 l/min, amorphous carbon by-produced during thebaking is not distilled off, causing reduction of the treatingtemperature for the resulting N-containing carbon alloy. When the flowrate is more than 2.0 l/min, the substrate would vaporize beforecarbonizing, resulting in a failure to produce an N-containing carbonalloy. To obtain a desired N-containing carbon alloy, theabove-described range of gas flow rate is recommended.

By performing the carbonization at high temperatures in a single stage,although the carbon alloy yield is reduced, the resulting carbon alloyhas a uniform crystallite size and therefore has metal atoms uniformlydistributed therein and maintains a highly active state. As a result, acarbon alloy with excellent oxygen reduction performance is produced.

The step of raising the temperature may be divided in two stages. Inthis case, during the first stage at relatively low temperatures,thermally instable substances, such as impurities and the solvent, areremoved. Providing a second stage of temperature rise allows forcontinuously performing decomposition and carbonization of the organicmaterial and also causing the decomposition product and the metal tomutually act to stabilize the metal in a more active state, for example,to stabilize Fe ions in a divalent state. As a result, a carbon alloywith excellent oxygen reduction performance is produced.

Furthermore, providing the second stage of temperature rise allows forincreasing the treating temperature in the subsequent carbonizationstep, thereby to provide a carbon alloy with a further regulated carbonstructure. As a result, the resulting carbon alloy will have improvedconductivity, high oxygen reduction performance, and improved catalystlife.

Raising the temperature in the first stage is to preheat the organicmaterial prior to the second stage while retaining only thermally stablestructures. Raising the temperature in the second stage σp to thecarbonization temperature is to obtain an appropriate carbon alloy. Ifthe temperature exceeds the carbonization temperature at this time,carbonization of the organic material may proceed excessively, which canresult in not only a failure to obtain an appropriate carbon alloy butalso reduction of yield.

The first stage temperature rise is preferably carried out in an inertatmosphere, such as a nitrogen gas atmosphere or a rare gas atmosphere.The inert gas atmosphere may contain oxygen in such an amount that doesnot cause combustion of the organic material. The inert gas atmospheremay be either in a closed system or in a semi-closed system with theinert gas flowing therethrough. The semi-closed system is preferred. Inthe semi-closed system, the gas flow rate is preferably 0.01 to 2.0l/min, more preferably 0.05 to 1.0 l/min, even more preferably 0.1 to0.5 l/min, per 36 mm inner diameter.

In the first stage of temperature rise, the organic material ispreferably heated σp to a temperature ranging from 100° to 500° C., morepreferably 150° to 400° C., to provide a uniformly precarbonizedmaterial.

The first stage of temperature rise may be achieved either by heatingthe organic material put in a carbonization chamber from roomtemperature to a predetermined temperature or by putting the organicmaterial in a carbonization chamber previously set at a predeterminedtemperature. The former manner is preferred. In the former case, thetemperature is preferably elevated at a constant rate. Morespecifically, the rate of temperature rise is preferably 1° C./min to1000° C./min, more preferably 1° C. to 500° C./min.

The second stage of temperature rise may be performed by continuouslyraising the temperature of the system from the temperature of the firststage to the carbonization temperature or once cooling the system toroom temperature followed by raising the temperature σp to thecarbonization temperature. In the case where the first stage oftemperature rise is once followed by cooling to room temperature, thecooled precarbonized material may be uniformly ground to powder, and thepowder may be molded into a desired shape.

The rate of temperature rise in the second stage is preferably 10°C./min to 1000° C./min, more preferably 10° C./min to 500° C./min. Thesecond stage temperature rise is preferably conducted in an inertatmosphere. In the case of a semi-closed system with a gas flow, theinert gas flow rate is preferably 0.01 to 2.0 l/min, more preferably0.05 to 1.0 l/min, even more preferably 0.1 to 0.5 l/min, per 36 mminner diameter. The gas flow rate in the second stage may be the same ordifferent from that in the first stage.

The step of carbonization is preferably carried out in the presence ofan activator. Carbonization at high temperatures in the presence of anactivator results in the formation of a carbon alloy with developedpores providing an increased surface area. As a result, the metal on thecarbon alloy is exposed, thereby, catalyst performance is improved. Thesurface area of the carbonized product is calculated from a nitrogen gasadsorption.

Examples of useful activators include, but are not limited to, at leastone selected from the group consisting of carbon dioxide, water vapor,air, oxygen, alkali metal hydroxides, zinc chloride, phosphoric acid,and mixtures thereof, with carbon dioxide, water vapor, air, oxygen, andmixtures thereof being preferred. A gaseous activator, such as carbondioxide or water vapor, is used in a concentration of 2 to 80 mol %,preferably 10 to 60 mol %, in the carbonizing atmosphere. A sufficientactivating effect is obtained with the activator concentrations of 2 mol% or more. When the activator concentration exceeds 80 mol %, excessiveactivation can result in considerable reduction of carbonization yield,a failure of efficient production of the carbonization product. A solidactivator, such as an alkali metal hydroxide, may be mixed as such withthe precarbonized material or dissolved or diluted with a solvent, suchas water, to make a solution, with which the carbon alloy precursor isimpregnated, or to make a slurry, which is kneaded into the carbon alloyprecursor. A liquid activator may be diluted with, e.g., water, and thecarbon alloy precursor is impregnated or mixed therewith.

After completion of the carbonization, the carbon alloy may be dopedwith nitrogen. Nitrogen doping may be performed by liquid phase doping,vapor phase doping, or vapor phase/liquid phase doping. For example, thecarbon alloy is heated in an ammonia gas atmosphere as a nitrogen sourceat 200° to 800° C. for 5 to 180 minutes to introduce nitrogen to thecarbon catalyst surface.

After the carbonization, the carbon alloy is cooled to room temperature.After the cooling step, the carbon alloy may be ground by any methodknown in the art, for example, by means of a ball mill.

(3) Applications

Applications of the N-containing carbon alloy of the invention include,but are not limited to, structural materials, electrode materials,filter materials, and catalyst materials. The N-containing carbon alloyis preferably used as an electrode material of electrical storagedevices, such as capacitors and lithium secondary batteries. It is morepreferably used as a carbon catalyst of fuel cells, zinc air batteries,and lithium air batteries featuring high ORR activity. The N-containingcarbon alloy is applicable to a membrane-electrode assembly (MEA) havinga solid polyelectrolyte membrane and catalyst layers adjacent to themembrane. The carbon catalyst of the N-containing carbon alloy may beincorporated into the catalyst layers. The MEA may be used in a fuelcell.

FIG. 1 is a schematic illustration of a fuel cell 10 having a carboncatalyst made of the carbon alloy of the invention. The carbon catalystis used in the anode and the cathode electrodes.

The fuel cell 10 includes a solid polyelectrolyte 14, a pair ofseparators 12 and 16, and a pair of electrode catalysts (i.e., an anodecatalyst (fuel electrode) 13 and a cathode catalyst (oxidant agentelectrode) 15), each pair are facing each other with the solidpolyelectrolyte 14 interposed therebetween. The solid polyelectrolyte 14may be a fluorine-based cation exchange resin membrane typified by aperfluorosulfonic resin membrane. The carbon catalyst of the inventionis disposed in contact with each side of the solid polyelectrolyte 14 toconstitute a fuel cell 10 having the carbon catalyst as the anodecatalyst 13 and the cathode catalyst 15. The carbon catalyst is formedon each side of the solid polyelectrolyte 14, and the anode catalyst 13and the cathode catalyst 15 are integrated on their electrode reactionlayer side with the respective sides of the solid polyelectrolyte 14 byhot pressing to make an MEA.

Conventional fuel cells have a porous sheet as a gas diffusion layer andas a current collector, such as carbon paper, disposed between eachelectrode catalyst and the adjacent separator. In contrast, the fuelcell 10 of FIG. 1 uses a carbon catalyst having a large specific surfacearea and good gas diffusion properties as an anode catalyst and acathode catalyst. By using the above described carbon catalyst aselectrode, the carbon catalyst has a function of gas diffusion when agas diffusion layer is not provided, and there can provide a fuel cellintegrated an anode and an cathode electrode catalyst 13 and 15 and agas diffusion layer. This achieves size and cost reduction of a fuelcell.

The separators 12 and 16 not only support the anode and the cathodecatalyst 13 and 15 but serve supply and exhaust of reactant gases, suchas fuel gas H₂ and oxidizing gas O₂. Upon supply of the reactant gasesto the anode and the cathode catalysts, a three-phase interface betweena vapor phase (reactant gases), a liquid phase (solid polyelectrolytemembrane), and a solid phase (catalyst of the electrodes) is formedalong the boundaries between the carbon catalyst of the two electrodesand the solid polyelectrolyte 14. An electrochemical reaction occurs atthe three-phase interface to generate direct current power. Theelectrochemical reactions proceed as follows.

Cathode side: O₂+4H⁺+4e ⁻→2H₂O

Anode side: H₂→2H⁺+2e ⁻

The H⁺ ions generated at the anode move through the solidpolyelectrolyte 14 toward the cathode, while electrons (e⁻) flow throughan external load toward the cathode. At the cathode, on the other hand,water forms as a result of reaction between oxygen in the oxidizing gas,the H⁺ ions coming from the anode side, and e⁻. Thus, the fuel cellgenerates a direct electric current from hydrogen and oxygen whileforming water.

An electrical storage device having the carbon catalyst having thecarbon alloy of the invention as an electrode material will then bedescribed. FIG. 2 schematically illustrates an electrical double-layercapacitor 20 having the carbon catalyst and therefore exhibiting highelectrical storage capacity.

The electrical double layer capacitor 20 shown in FIG. 2 includes a pairof polarizable electrodes (a first electrode 21 and a second electrode22) separated by a separator 23. These capacitor components are sealedin a package composed of a case 24 b and a cap 24 a. The first electrode21 and the second electrode 22 are connected to the cap 24 a and thecase 24 b, respectively, via respective current collectors 25. Theseparator 23 is impregnated with an electrolyte. The cap 24 a and thecase 24 b are swaged to each other via a gasket 26 for electricalinsulation therebetween.

The carbon catalyst of the invention is applied to the first electrode21 and the second electrode 22 to complete an electrical double layercapacitor having the carbon catalyst as electrode material. The carboncatalyst described has a fibrous structure formed of nanoshell carbonparticles. The fibers are of nanometer diameter to provide a largespecific surface area, thereby providing a large electrode interfacewhere electrical charges are stored in the capacitor. The carboncatalyst is electrochemically inert to the electrolyte and hasappropriate electrical conductivity. Therefore, applying the carboncatalyst to the electrodes of capacitors brings about improvement inelectrostatic capacity per electrode unit volume.

Similarly to the application to the capacitor, the carbon catalyst ofthe invention is also applicable as an electrode material formed of acarbon material, such as a negative electrode material of lithium ionsecondary batteries. Having a large specific surface area, the carboncatalyst provides a secondary battery with a large storage capacity.

An embodiment of application of the carbon alloy of the invention as asubstitute for a noble metal-based (e.g., Pt-based) environmentalcatalyst will now be described.

An environmental catalyst having a catalyst material containing a noblemetal-based (e.g., Pt-based) material or a composite thereof has beenused as a catalyst for exhaust gas purification, which is to removecontaminants (chiefly gaseous substances) from contaminated air bydecomposition or otherwise. The above described carbon catalyst isuseful as a substitute for this type of catalyst. The carbon catalysthas a function to decompose substances to be removed, such ascontaminants, because of its ORR catalyzing action. Accordingly, anenvironmental catalyst is provided at a lower cost by using the carboncatalyst in place of expensive noble metals such as platinum.Furthermore, having a large specific surface area, the carbon catalysthas an increased area capable of decomposing substances to be removedper unit volume, thereby providing an environmental catalyst withexcellent decomposing function per unit volume.

The carbon catalyst may also be used as a catalyst carrier on which anoble metal-based (e.g., Pt-based) material used in conventionalenvironmental catalysts is supported either alone or in the form of acomposite thereof, thereby establishing an environmental catalyst withimproved catalyst activity, such as decomposing activity. Theenvironmental catalyst having the carbon catalyst is useful not only asa catalyst for exhaust gas purification as described but also as acatalyst for purifying water.

The carbon alloy of the invention is also useful as a catalyst for awide range of chemical reactions, especially as a substitute forplatinum catalysts. That is, the above described carbon catalyst isuseful as a substitute for general processing catalysts containing anoble metal, e.g., platinum, in chemical industries. Without usingexpensive noble metals, such as platinum, the carbon alloy provideslow-cost catalysts for chemical reaction processes. Having a largespecific surface area, the carbon catalyst provides a catalyst forchemical reaction processes with excellent chemical reaction efficiencyper unit volume.

Examples of the carbon catalysts for chemical reactions includecatalysts for hydrogenation, catalysts for dehydrogenation, catalystsfor oxidation, catalysts for polymerization, catalysts for reformingreaction, and catalysts for steam reforming. More specifically, thecarbon catalyst is applicable to various chemical reactions withreference to the literature relating to catalysts, such as T. Shirosaki& N. Tohdo, SHOKUBAI CYOSEI, Kodansha, 1975.

The present invention will now be illustrated in greater detail withreference to Examples, but it should be understood that the invention isnot deemed to be limited thereto.

Example 1 Synthesis of Carbon Material (1C) from PR 254 (1)Infusibilization and Carbonization

Pigment Red 254 (from Tokyo Chemical Industry Co., Ltd.; hereinafter “PR254”) (1.001 g) is weighed into a quartz boat. The quartz boat is placedin the middle of a quartz tube (outer diameter: 4.0 cm; inner diameter:3.6 cm) inserted in a tubular furnace. Nitrogen is made to flow at arate of 300 ml/min for 30 minutes at room temperature. The PR 254 isheated at a rate of temperature rise of 1° C./min from 30° C. to 300° C.and then at 10° C./min from 300° C. to 800° C., maintained at 800° C.for 1 hour, and cooled to room temperature over a period of 3 hours toobtain 0.346 g of a carbon material (1B).

(2) Grinding

The carbon material (1B) is ground in an agate mortar to obtain a carbonmaterial (1C).

Molecular formula: C₁₈H₁₀Cl₂N₂O₂Molecular weight: 357.190Elemental analysis (calcd.): C, 60.53; H, 2.82; Cl, 19.85; N, 7.84; O,8.96.

Comparative Example 1 Synthesis of Carbon Material (C1C) from PhOHInfusibilization and Carbonization

Phenol (PhOH) (from Wako Pure Chemical Industries, Ltd.) (1.000 g) isweighed into a quartz boat. The quartz boat is placed in the middle of aquartz tube (outer diameter: 4.0 cm; inner diameter: 3.6 cm) inserted ina tubular furnace. Nitrogen is made to flow at a rate of 300 ml/min for30 minutes at room temperature. The PhOH is heated at a rate oftemperature rise of 1° C./min from 30° C. to 300° C. and then at 10°C./min from 300° C. to 700° C., maintained at 700° C. for 1 hour, andcooled to room temperature over a period of 3 hours, resulting in afailure to obtain a carbon material.

The same procedures are repeated, except for replacing phenol withphthalonitrile (from Wako Pure Chemical Industries, Ltd.), resulting inthe same failure.

Phenol:

Molecular formula: C₆H₆OMolecular weight: 94.11Elemental analysis (calcd.): C, 76.57; H, 6.43; N, 0.00; O, 17.00.

Phthalonitrile:

Molecular formula: C₈H₄N₂Molecular weight: 128.13Elemental analysis (calcd.): C, 74.99; H, 3.15; N, 21.86.

Comparative Example 2 Synthesis of Carbon Material (C2C) from MeCNInfusibilization and Carbonization

Acetonitrile (MeCN) (from Wako Pure Chemical Industries, Ltd.) (1.000 g)is weighed into a quartz boat. The quartz boat is placed in the middleof a quartz tube (outer diameter: 4.0 cm; inner diameter: 3.6 cm)inserted in a tubular furnace. Nitrogen is made to flow at a rate of 300ml/min for 30 minutes at room temperature. The MeCN is heated at a rateof temperature rise of 1° C./min from 30° C. to 300° C. and then at 10°C./min from 300° C. to 700° C., maintained at 700° C. for 1 hour, andcooled to room temperature over a period of 3 hours, resulting in afailure to obtain a carbon material.

Acetonitrile:

Molecular formula: C₂H₃NMolecular weight: 41.05Elemental analysis (calcd.): C, 58.51; H, 7.37; N, 34.12.

Example 2 Synthesis of Carbon Material (2C) from Iron (III) ChlorideHexahydrate/PR 202 Mixture (1) Preparation of Iron (III) ChlorideHexahydrate/PR 202 Mixture

To 4.0 g of 2,9-dichloroquinacridone (CINQUASIA Magenta P, from BASFJapan Ltd.) (hereinafter PR 202) is added 1.017 g of iron (III) chloridehexahydrate (from Wako Pure Chemical Industries, Ltd.) and mixed in anagate mortar to prepare an iron (III) chloride hexahydrate/PR 202mixture (2A).

(2) Infusibilization and Carbonization

The mixture (2A) (1.002 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (2A) is heated at a rate of temperature rise of 1° C./min from30° C. to 300° C. and then at 10° C./min from 300° C. to 700° C.,maintained at 700° C. for 1 hour, and cooled to room temperature over aperiod of 3 hours to obtain 0.529 g of a carbon material (2B).

(3) Grinding and Acid Cleaning

The carbon material (2B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (2C).

Molecular formula: C₂₀H₁₀Cl₂N₂O₂Molecular weight: 381.212Elemental analysis (calcd.): C, 63.01; H, 2.64; Cl, 18.60; N, 7.35; O,8.39.

Example 3 Synthesis of Carbon Material (3C) from Iron (III) ChlorideHexahydrate/PO 71 Mixture (1) Preparation of Iron (III) ChlorideHexahydrate/PO 71 Mixture

To 4.0 g of Pigment Orange 71 (CROMOPHTAL DPP ORANGE TR from BASF JapanLtd.) (hereinafter PO 71) is added 1.065 g of iron (III) chloridehexahydrate (Wako Pure Chemical Industries, Ltd.) and mixed in an agatemortar to prepare an iron (III) chloride hexahydrate/PO 71 mixture (3A).

(2) Infusibilization and Carbonization

The mixture (3A) (1.006 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (3A) is heated at a rate of temperature rise of 1° C./min from30° C. to 300° C. and then at 10° C./min from 300° C. to 700° C.,maintained at 700° C. for 1 hour, and cooled to room temperature over aperiod of 30 minutes to obtain 0.390 g of a carbon material (3B).

(3) Grinding and Acid Cleaning

The carbon material (3B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (3C).

Molecular formula: C₂₀H₁₀N₄O₂Molecular weight: 338.319Elemental analysis (calcd.): C, 71.00; H, 2.98; N, 16.56; O, 9.46.

Example 4 Synthesis of Carbon Material (4C) from Iron (III) Chloride/PR254 Mixture (1) Preparation of Iron (III) Chloride/PR 254 Mixture

To 4.0 g of PR 254 (IRGAPHOR RED BT-CF, from BASF Japan Ltd.) is added0.606 g of iron (III) chloride (from Wako Pure Chemical Industries,Ltd.) and mixed in an agate mortar to prepare an iron (III) chloride/PR254 mixture (4A).

(2) Infusibilization and Carbonization

The mixture (4A) (1.003 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (4A) is heated at a rate of temperature rise of 1° C./min from30° C. to 300° C. and then at 10° C./min from 300° C. to 700° C.,maintained at 700° C. for 1 hour, and cooled to room temperature over aperiod of 3 hours to obtain 0.372 g of a carbon material (4B).

(3) Grinding and Acid Cleaning

The carbon material (4B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (4C).

Example 5 Synthesis of Carbon Material (5C) from Iron (III) ChlorideHexahydrate/PR 254 Mixture (1) Preparation of Iron (III) ChlorideHexahydrate/PR 254 Mixture

To 3.00 g of PR 254 (IRGAPHOR RED BT-CF, from BASF Japan Ltd.) is added1.614 g of iron (III) chloride hexahydrate (from Wako Pure ChemicalIndustries, Ltd.) and mixed in an agate mortar to prepare an iron (III)chloride hexahydrate/PR 254 mixture (5A).

(2) Infusibilization and Carbonization

The mixture (5A) (1.010 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (5A) is heated at a rate of temperature rise of 1° C./min from30° C. to 300° C. and then at 10° C./min from 300° C. to 800° C.,maintained at 800° C. for 1 hour, and cooled to room temperature over aperiod of 3 hours to obtain 0.341 g of a carbon material (5B).

(3) Grinding and Acid Cleaning

The carbon material (5B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (5C).

Example 6 Synthesis of Carbon Material (6C) from Iron (III) ChlorideHexahydrate/PR 254 Latent Pigment Mixture (1) Preparation of Iron (III)Chloride Hexahydrate/PR 254 Latent Pigment Mixture

Iron (III) chloride hexahydrate (from Wako Pure Chemical Industries,Ltd.) (0.544 g) is added to 4.00 g of a PR 254 latent pigment, which iscompound (12) shown in JP 2010-83982A, para. [0072] (hereinafter “PR254-LP”) and mixed in an agate mortar to prepare an iron (III) chloridehexahydrate/PR 254-LP mixture (6A).

(2) Infusibilization and Carbonization

The mixture (6A) (1.013 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (6A) is heated at a rate of temperature rise of 1° C./min from30° C. to 300° C. and then at 10° C./min from 300° C. to 700° C.,maintained at 700° C. for 1 hour, and cooled to room temperature over aperiod of 30 minutes to obtain 0.259 g of a carbon material (6B).

(3) Grinding and Acid Cleaning

The carbon material (6B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (6C).

Molecular formula: C₂₈H₃₀O₂N₂O₂Molecular weight: 497.456Elemental analysis (calcd.): C, 67.60; H, 6.08; Cl, 14.25; N, 5.63; O,6.43.

Example 7 Synthesis of Carbon Material (7C) from Iron (III) ChlorideHexahydrate/PR 254 Mixture (1) Preparation of Iron (III) ChlorideHexahydrate/PR 254 Mixture

To 3.0 g of PR 254 (IRGAPHOR RED BT-CF, from BASF Japan Ltd.) is added0.757 g of iron (III) chloride hexahydrate (from Wako Pure ChemicalIndustries, Ltd.) and mixed in an agate mortar to prepare an Iron (III)Chloride Hexahydrate/PR 254 mixture (7A).

(2) Infusibilization and Carbonization

The mixture (7A) (1.003 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (7A) is heated at a rate of temperature rise of 1° C./min from30° C. to 300° C. and then at 10° C./min from 300° C. to 700° C.,maintained at 700° C. for 1 hour, and cooled to room temperature over aperiod of 30 minutes to obtain 0.372 g of a carbon material (7B).

(3) Grinding and Acid Cleaning

The carbon material (7B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (7C).

Example 8 Synthesis of Carbon Material (8C) from Iron (II) ChlorideTetrahydrate/PR 254 Mixture

(1) Preparation of Iron (II) Chloride Tetrahydrate/PR 254 mixture

To 4.0 g of PR 254 (IRGAPHOR RED BT-CF, from BASF Japan Ltd.) is added0.742 g of iron (II) chloride tetrahydrate (from Wako Pure ChemicalIndustries, Ltd.) and mixed in an agate mortar to prepare an iron (II)chloride tetrahydrate/PR 254 mixture (8A).

(2) Infusibilization and Carbonization

The mixture (8A) (1.005 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (8A) is heated at a rate of temperature rise of 1° C./min from30° C. to 300° C. and then at 10° C./min from 300° C. to 700° C.,maintained at 700° C. for 1 hour, and cooled to room temperature over aperiod of 3 hours to obtain 0.390 g of a carbon material (8B).

(3) Grinding and Acid Cleaning

The carbon material (8B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (8C).

Example 9 Synthesis of Carbon Material (9C) from Iron (III) ChlorideHexahydrate/4,5-Dichlorophthalonitrile (DCP) Mixture (1) Preparation ofIron (III) Chloride Hexahydrate/DCP Mixture

To 5.04 g of 4,5-dichlorophthalonitrile (DCP) (from Tokyo ChemicalIndustry Co., Ltd.) is added 1.15 g of iron (III) chloride hexahydrate(from Wako Pure Chemical Industries, Ltd.) and mixed in an agate mortarto prepare an iron (III) chloride hexahydrate/DCP mixture (9A).

(2) Infusibilization and Carbonization

The mixture (9A) (1.022 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (9A) is heated at a rate of temperature rise of 500° C./min from30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled to roomtemperature over a period of 30 minutes to obtain 0.250 g of a carbonmaterial (9B).

(3) Grinding and Acid Cleaning

The carbon material (9B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (9C).

4,5-Dichlorophthalonitrile

Molecular formula: C₈H₂N₂Cl₂Molecular weight: 197.02Elemental analysis (calcd.): C, 48.77; H, 1.02; N, 14.22; Cl, 35.99.

Comparative Example 3 Synthesis of Carbon Material (C3C) from IronPhthalocyanine (Fe-Pc) (1) Infusibilization and Carbonization

Iron phthalocyanine (Fe-Pc) (from Tokyo Chemical Industry Co., Ltd.)(1.007 g) is weighed into a quartz boat. The quartz boat is placed inthe middle of a quartz tube (outer diameter: 4.0 cm; inner diameter: 3.6cm) inserted in a tubular furnace. Nitrogen is made to flow at a rate of300 ml/min for 30 minutes at room temperature. The Fe-Pc is heated at arate of temperature rise of 1° C./min from 30° C. to 300° C. and then at10° C./min from 300° C. to 700° C., maintained at 700° C. for 1 hour,and cooled to room temperature over a period of 3 hours to obtain 0.684g of a carbon material (C3B).

(2) Grinding and Acid Cleaning

The carbon material (C3B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (C3C).

Molecular formula: C₃₂H₁₆FeN₈Molecular weight: 568.368Elemental analysis (calcd.): C, 67.62; H, 2.84; Fe, 9.83; N, 19.71.

Example 10 Synthesis of Carbon Material (10C) from Cobalt (II) ChlorideHexahydrate/4,5-Dichlorophthalonitrile (DCP) Mixture (1) Preparation ofCobalt (II) Chloride Hexahydrate/DCP Mixture

To 4.00 g of 4,5-dichlorophthalonitrile (DCP) (from Tokyo ChemicalIndustry Co., Ltd.) is added 0.805 g of cobalt (II) chloride hexahydrate(from Wako Pure Chemical Industries, Ltd.) and mixed in an agate mortarto prepare a cobalt (II) chloride hexahydrate/DCP mixture (10A).

(2) Infusibilization and Carbonization

The mixture (10A) (1.032 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (10A) is heated at a rate of temperature rise of 5° C./min from30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled to roomtemperature over a period of 3 hours to obtain 0.323 g of a carbonmaterial (10B).

(3) Grinding and Acid Cleaning

The carbon material (10B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (10C).

Example 11 Synthesis of Carbon Material (11C) from Cobalt (II) ChlorideHexahydrate/PR 122 Mixture (1) Preparation of Cobalt (II) ChlorideHexahydrate/PR 122 Mixture

To 4.0 g of 2,9-dimethylquinacridone (Chromophtal Pink PT, from BASFJapan Ltd.) (hereinafter PR 122) is added 1.016 g of cobalt (II)chloride hexahydrate (from Wako Pure Chemical Industries, Ltd.) andmixed in an agate mortar to prepare a cobalt (II) chloridehexahydrate/PR 122 mixture (11A).

(2) Infusibilization and Carbonization

The mixture (11A) (1.003 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (11A) is heated at a rate of temperature rise of 1° C./min from30° C. to 300° C. and then at 10° C./min from 300° C. to 700° C.,maintained at 700° C. for 1 hour, and cooled to room temperature over aperiod of 3 hours to obtain 0.670 g of a carbon material (11B).

(3) Grinding and Acid Cleaning

The carbon material (11B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (11C).

Molecular formula: C₂₂H₁₆N₂O₂Molecular weight: 340.375Elemental analysis (calcd.): C, 77.63; H, 4.74; N, 8.23; O, 9.40.

Example 12 Synthesis of Carbon Material (12C) from Cobalt (II) ChlorideHexahydrate/4-Hydroxyphthalonitrile (4-HPN) Mixture (1) Preparation ofCobalt (II) Chloride Hexahydrate/4-HPN Mixture

To 4.26 g of 4-hydroxyphthalonitrile (4-HPN) (from Tokyo ChemicalIndustry Co., Ltd.) is added 1.10 g of cobalt (II) chloride hexahydrate(from Wako Pure Chemical Industries, Ltd.) and mixed in an agate mortarto prepare a cobalt (II) chloride hexahydrate/4-HPN mixture (12A).

(2) Infusibilization and Carbonization

The mixture (12A) (1.003 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (12A) is heated at a rate of temperature rise of 500° C./minfrom 30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled toroom temperature over a period of 30 minutes to obtain 0.503 g of acarbon material (12B).

(3) Grinding and Acid Cleaning

The carbon material (12B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (12C).

4-Hydroxyphthalonitrile

Molecular formula: C₈H₄N₂OMolecular weight: 144.13Elemental analysis (calcd.): C, 66.67; H, 2.80; N, 19.44; O, 11.10.

Example 13 Synthesis of Carbon Material (13C) from Cobalt (II) ChlorideHexahydrate/4,5-Dihydroxybenzonitrile (4,5-DHBN) Mixture

(1) Preparation of cobalt (II) chloride hexahydrate/4,5-DHBN mixture

To 5.0 g of 4,5-dihydroxybenzonitrile (4,5-DHBN) (from Wako PureChemical Industries, Ltd.) is added 1.47 g of cobalt (II) chloridehexahydrate (from Wako Pure Chemical Industries, Ltd.) and mixed in anagate mortar to prepare a cobalt (II) chloride hexahydrate/4,5-DHBNmixture (13A).

(2) Infusibilization and Carbonization

The mixture (13A) (1.008 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (13A) is heated at a rate of temperature rise of 500° C./minfrom 30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled toroom temperature over a period of 30 minutes to obtain 0.174 g of acarbon material (13B).

(3) Grinding and Acid Cleaning

The carbon material (13B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (13C).

4,5-Dihydroxybenzonitrile

Molecular formula: C₇H₅NO₂Molecular weight: 135.12Elemental analysis (calcd.): C, 62.22; H, 3.73; N, 10.37; O, 23.37.

Example 14 Synthesis of Carbon Material (14C) from Cobalt (II) ChlorideHexahydrate/Phthalonitrile (PN) Mixture (1) Preparation of Cobalt (II)Chloride Hexahydrate/PN Mixture

To 4.00 g of phthalonitrile (PN) (from Tokyo Chemical Industry Co.,Ltd.) is added 1.24 g of cobalt (II) chloride hexahydrate (from WakoPure Chemical Industries, Ltd.) and mixed in an agate mortar to preparea cobalt (II) chloride hexahydrate/PN mixture (14A).

(2) Infusibilization and Carbonization

The mixture (14A) (1.002 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (14A) is heated at a rate of temperature rise of 500° C./minfrom 30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled toroom temperature over a period of 30 minutes to obtain 0.092 g of acarbon material (14B).

(3) Grinding and Acid Cleaning

The carbon material (14B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (14C).

Phthalonitrile:

Molecular formula: C₈H₄N₂Molecular weight: 128.13Elemental analysis (calcd.): C, 74.99; H, 3.15; N, 21.86.

Example 15 Synthesis of Carbon Material (15C) from Cobalt (II) ChlorideHexahydrate/Vulcan Black (VB)/PN Mixture (1) Preparation of Cobalt (II)Chloride Hexahydrate/VB/PN Mixture

To 4.00 g of phthalonitrile (PN) (from Tokyo Chemical Industry Co.,Ltd.) is added 1.24 g of cobalt (II) chloride hexahydrate (from WakoPure Chemical Industries, Ltd.) and mixed in an agate mortar. To 2.00 gof the resulting mixture is further added 2.00 g of Vulcan Black (VB)(XC-72, from Cabot Corporation) to prepare a cobalt (II) chloridehexahydrate/VB/PN mixture (15A).

(2) Infusibilization and Carbonization

The mixture (15A) (1.004 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (15A) is heated at a rate of temperature rise of 500° C./minfrom 30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled toroom temperature over a period of 30 minutes to obtain 0.546 g of acarbon material (15B).

(3) Grinding and Acid Cleaning

The carbon material (15B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (15C).

Example 16 Synthesis of Carbon Material (16C) from Cobalt (II) ChlorideHexahydrate/VB/4-Hydroxyphthalonitrile (4-HPN) Mixture (1) Preparationof Cobalt (II) Chloride Hexahydrate/VB/4-HPN Mixture

To 4.26 g of 4-hydroxyphthalonitrile (4-HPN) (from Tokyo ChemicalIndustry Co., Ltd.) is added 1.10 g of cobalt (II) chloride hexahydrate(from Wako Pure Chemical Industries, Ltd.) and mixed in an agate mortar.To 2.00 g of the resulting mixture is further added 2.00 g of VulcanBlack (VB) (XC-72, from Cabot) to prepare a cobalt (II) chloridehexahydrate/VB/4-HPN mixture (16A).

(2) Infusibilization and Carbonization

The mixture (16A) (1.004 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (16A) is heated at a rate of temperature rise of 10° C./min from30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled to roomtemperature over a period of 3 hours to obtain 0.667 g of a carbonmaterial (16B).

(3) Grinding and Acid Cleaning

The carbon material (16B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (16C).

Example 17 Synthesis of Carbon Material (17C) from Cobalt (II) ChlorideHexahydrate/Malononitrile (MN) Mixture (1) Preparation of Cobalt (II)Chloride Hexahydrate/MN Mixture

To 5.00 g of malononitrile (MN) (from Wako Pure Chemical Industries,Ltd.) is added 3.00 g of cobalt (II) chloride hexahydrate (from WakoPure Chemical Industries, Ltd.) and mixed in an agate mortar to preparea cobalt (II) chloride hexahydrate/MN mixture (17A).

(2) Infusibilization and Carbonization

The mixture (17A) (1.042 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (17A) is heated at a rate of temperature rise of 500° C./minfrom 30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled toroom temperature over a period of 30 minutes to obtain 0.239 g of acarbon material (17B).

(3) Grinding and Acid Cleaning

The carbon material (17B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (17C).

Malononitrile:

Molecular formula: C₃H₂N₂Molecular weight: 66.06Elemental analysis (calcd.): C, 54.54; H, 3.05; N, 42.41.

Example 18 Synthesis of Carbon Material (18C) from Cobalt (II) ChlorideHexahydrate/2-Cyanobenzamide (2-CBA) Mixture

(1) Preparation of cobalt (II) chloride hexahydrate/2-CBA mixture

To 5.13 g of 2-cyanobenzamide (2-CBA) (from Tokyo Chemical Industry Co.,Ltd.) is added 1.39 g of cobalt (II) chloride hexahydrate (from WakoPure Chemical Industries, Ltd.) and mixed in an agate mortar to preparea cobalt (II) chloride hexahydrate/2-CBA mixture (18A).

(2) Infusibilization and Carbonization

The mixture (18A) (1.023 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (18A) is heated at a rate of temperature rise of 5° C./min from30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled to roomtemperature over a period of 30 minutes to obtain 0.260 g of a carbonmaterial (18B).

(3) Grinding and Acid Cleaning

The carbon material (18B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (18C).

2-Cyanobenzamide

Molecular formula: C₈H₆N₂OMolecular weight: 66.06Elemental analysis (calcd.): C, 65.75; H, 4.14; N, 19.17; O, 10.95.

Example 19 Synthesis of Carbon Material (19C) from Cobalt (II) ChlorideHexahydrate/3-Cyanobenzamide (3-CBA) Mixture (1) Preparation of Cobalt(II) Chloride Hexahydrate/3-CBA Mixture

To 4.00 g of 3-cyanobenzamide (3-CBA) (compound 16a shown in J. Chem.Soc., Perkin Trans. I. 13, 1679 (1994)) is added 1.085 g of cobalt (II)chloride hexahydrate (from Wako Pure Chemical Industries, Ltd.) andmixed in an agate mortar to prepare a cobalt (II) chloridehexahydrate/3-CBA mixture (19A).

(2) Infusibilization and Carbonization

The mixture (19A) (1.003 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (19A) is heated at a rate of temperature rise of 500° C./minfrom 30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled toroom temperature over a period of 30 minutes to obtain 0.075 g of acarbon material (19B).

(3) Grinding and Acid Cleaning

The carbon material (19B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (19C).

3-Cyanobenzamide

Molecular formula: C₈H₆N₂OMolecular weight: 66.06Elemental analysis (calcd.): C, 65.75; H, 4.14; N, 19.17; O, 10.95.

Example 20 Synthesis of Carbon Material (20C) from Cobalt (II) ChlorideHexahydrate/4-Chloronitrobenzonitrile (Cl-Ph-CN) Mixture (1) Preparationof Cobalt (II) Chloride Hexahydrate/Cl-Ph-CN Mixture

To 4.0 g of 4-chloronitrobenzonitrile (Cl-Ph-CN) (from Tokyo ChemicalIndustry Co., Ltd.) is added 1.15 g of cobalt (II) chloride hexahydrate(from Wako Pure Chemical Industries, Ltd.) and mixed in an agate mortarto prepare a cobalt (II) chloride hexahydrate/Cl-Ph-CN mixture (20A).

(2) Infusibilization and Carbonization

The mixture (20A) (1.012 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (20A) is heated at a rate of temperature rise of 500° C./minfrom 30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled toroom temperature over a period of 30 minutes to obtain 0.0526 g of acarbon material (20B).

(3) Grinding and Acid Cleaning

The carbon material (20B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (20C).

4-Chloronitrobenzonitrile

Molecular formula: C₇H₄C1Molecular weight: 137.57Elemental analysis (calcd.): C, 61.12; H, 2.93; N, 10.18; Cl, 25.77.

Example 21 Synthesis of Carbon Material (21C) from Cobalt (II) ChlorideHexahydrate/Ketjen Black (KB)/Cl-Ph-CN Mixture (1) Preparation of Cobalt(II) Chloride Hexahydrate/Kb/Cl-Ph-CN Mixture

To 4.0 g of 4-chloronitrobenzonitrile (Cl-Ph-CN) (from Tokyo ChemicalIndustry Co., Ltd.) is added 1.15 g of cobalt (II) chloride hexahydrate(from Wako Pure Chemical Industries, Ltd.) and mixed in an agate mortar.To 2.0 g of the resulting mixture is further added 2.0 g of Ketjen black(KB) (EC300J, from Lion Corp.) to prepare a cobalt (II) chloridehexahydrate/KB/Cl-Ph-CN mixture (21A).

(2) Infusibilization and Carbonization

The mixture (21A) (0.514 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (21A) is heated at a rate of temperature rise of 500° C./minfrom 30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled toroom temperature over a period of 30 minutes to obtain 0.292 g of acarbon material (21B).

(3) Grinding and Acid Cleaning

The carbon material (21B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (21C).

Example 22 Synthesis of Carbon Material (22C) from Cobalt (II) ChlorideHexahydrate/VB/DCP Mixture

(1) Preparation of cobalt (II) chloride hexahydrate/VB/DCP mixture

To 4.00 g of 4,5-dichlorophthalonitrile (DCP) (from Tokyo ChemicalIndustry Co., Ltd.) is added 0.805 g of cobalt (II) chloride hexahydrate(from Wako Pure Chemical Industries, Ltd.) and mixed in an agate mortar.To 2.0 g of the resulting mixture is further added 2.0 g of Vulcan Black(VB) (XC-72, from Cabot Corporation) to prepare a cobalt (II) chloridehexahydrate/VB/DCP mixture (22A).

(2) Infusibilization and Carbonization

The mixture (22A) (1.003 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (22A) is heated at a rate of temperature rise of 10° C./min from30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled to roomtemperature over a period of 30 minutes to obtain 0.632 g of a carbonmaterial (22B).

(3) Grinding and Acid Cleaning

The carbon material (22B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (22C).

Example 23 Synthesis of Carbon Material (23C) from Cobalt Chloride (II)Hexahydrate/PR 254 Latent Pigment (PR 254-LP) Mixture (1) Preparation ofCobalt (II) Chloride Hexahydrate/PR 254-LP Mixture

Cobalt (II) chloride hexahydrate (from Wako Pure Chemical Industries,Ltd.) (0.479 g) is added to 4.00 g of PR 254 latent pigment (PR 254-LP),which is compound (12) shown in [chemical formula 24] of para. [0072]and [chemical formula 17] of para. [0158] in JP 2010-83982A, and mixedin an agate mortar to prepare a cobalt (II) chloride hexahydrate/PR254-LP mixture (23A).

(2) Infusibilization and Carbonization

The mixture (23A) (0.996 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (23A) is heated at a rate of temperature rise of 1° C./min from30° C. to 300° C. and then at 10° C./min from 300° C. to 700° C.,maintained at 700° C. for 1 hour, and cooled to room temperature over aperiod of 3 hours to obtain 0.270 g of a carbon material (23B).

(3) Grinding and Acid Cleaning

The carbon material (23B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (23C).

Example 24 Synthesis of Carbon Material (24C) from Cobalt (II) NitrateHexahydrate/PR 254 Mixture (1) Preparation of Cobalt (II) NitrateHexahydrate/PR 254 Mixture

To 4.0 g of PR 254 (IRGAPHOR RED BT-CF, from BASF Japan Ltd.) is added1.09 g of cobalt (II) nitrate hexahydrate (from Wako Pure ChemicalIndustries, Ltd.) and mixed in an agate mortar to prepare a cobalt (II)nitrate hexahydrate/PR 254 mixture (24A).

(2) Infusibilization and Carbonization

The mixture (24A) (1.004 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (24A) is heated at a rate of temperature rise of 1° C./min from30° C. to 300° C. and then at 10° C./min from 300° C. to 700° C.,maintained at 700° C. for 1 hour, and cooled to room temperature over aperiod of 3 hours to obtain 0.366 g of a carbon material (24B).

(3) Grinding and Acid Cleaning

The carbon material (24B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (24C).

Example 25 Synthesis of Carbon Material (25C) from Cobalt (II) ChlorideHexahydrate/PR 254 Mixture (1) Preparation of Cobalt (II) ChlorideHexahydrate/PR 254 Mixture

To 4.0 g of PR 254 (IRGAPHOR RED BT-CF, from BASF Japan Ltd.) is added0.888 g of cobalt (II) chloride hexahydrate (from Wako Pure ChemicalIndustries, Ltd.) and mixed in an agate mortar to prepare a cobalt (II)chloride hexahydrate/PR 254 mixture (25A).

(2) Infusibilization and Carbonization

The mixture (25A) (1.000 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (25A) is heated at a rate of temperature rise of 1° C./min from30° C. to 300° C. and then at 10° C./min from 300° C. to 800° C.,maintained at 800° C. for 1 hour, and cooled to room temperature over aperiod of 30 minutes to obtain 0.328 g of a carbon material (25B).

(3) Grinding and Acid Cleaning

The carbon material (25B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (25C).

Example 26 Synthesis of Carbon Material (26C) from Cobalt (II) ChlorideHexahydrate/PY 138 Mixture (1) Preparation of Cobalt (II) ChlorideHexahydrate/PY 138 Mixture

To 4.0 g of Pigment Yellow 138 (PY 138) (PALIOTOL YELLOW P09 60, fromBASF Japan Ltd.) is added 0.457 g of cobalt (II) chloride hexahydrate(from Wako Pure Chemical Industries, Ltd.) and mixed in an agate mortarto prepare a cobalt (II) chloride hexahydrate/PY 138 mixture (26A).

(2) Infusibilization and Carbonization

The mixture (26A) (1.041 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (26A) is heated at a rate of temperature rise of 10° C./min from30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled to roomtemperature over a period of 3 hours to obtain 0.559 g of a carbonmaterial (26B).

(3) Grinding and Acid Cleaning

The carbon material (26B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (26C).

Molecular formula: C₂₆H₆Cl₈N₂O₄Molecular weight: 693.961Elemental analysis (calcd.): C, 45.00; H, 0.87; Cl, 40.87; N, 4.04; O,9.22.

Example 27 Synthesis of Carbon Material (27C) from Cobalt (II) ChlorideHexahydrate/PY 185 Mixture (1) Preparation of Cobalt (II) ChlorideHexahydrate/PY 185 Mixture

To 3.0 g of Pigment Yellow 185 (PY 185) (PALIOTOL YELLOW P11 55, fromBASF Japan Ltd.) is added 0.701 g of cobalt (II) chloride hexahydrate(from Wako Pure Chemical Industries, Ltd.) and mixed in an agate mortarto prepare a cobalt (II) chloride hexahydrate/PY 185 mixture (27A).

(2) Infusibilization and Carbonization

The mixture (27A) (1.031 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (27A) is heated at a rate of temperature rise of 10° C./min from30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled to roomtemperature over a period of 3 hours to obtain 0.362 g of a carbonmaterial (27B).

(3) Grinding and Acid Cleaning

The carbon material (27B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (27C).

Molecular formula: C₁₆H₁₁N₅O₄Molecular weight: 337.290Elemental analysis (calcd.): C, 56.98; H, 3.29; N, 20.76; O, 18.97.

Example 34 Synthesis of Carbon Material (34C) from Cobalt (II) ChlorideHexahydrate/PY 109 Mixture (1) Preparation of Cobalt (II) ChlorideHexahydrate/PY 109 Mixture

To 4.00 g of Pigment Yellow 109 (PY 109) (IRGAZIN YELLOW 2GLTE, fromBASF Japan Ltd.) is added 0.484 g of cobalt (II) chloride hexahydrate(from Wako Pure Chemical Industries, Ltd.) and mixed in an agate mortarto prepare a cobalt (II) chloride hexahydrate/PY 109 mixture (34A).

(2) Infusibilization and Carbonization

The mixture (34A) (1.007 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (34A) is heated at a rate of temperature rise of 10° C./min from30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled to roomtemperature over a period of 3 hours to obtain 0.506 g of a carbonmaterial (34B).

(3) Grinding and Acid Cleaning

The carbon material (34B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 110° C. for 1 hour to obtain an acidcleaned carbon material (34C).

Molecular formula: C₂₃H₈Cl₈N₄O₂Molecular weight: 655.959Elemental analysis (calcd.): C, 42.11; H, 1.23; Cl, 43.24; N, 8.54; O,4.88.

Example 35 Synthesis of Carbon Material (35C) from Cobalt (II) ChlorideHexahydrate/PY 110 Mixture (1) Preparation of Cobalt (II) ChlorideHexahydrate/PY 110 Mixture

To 4.00 g of Pigment Yellow 110 (PY 110) (IRGAZIN YELLOW 2RLT, from BASFJapan Ltd.) is added 0.494 g of cobalt (II) chloride hexahydrate (fromWako Pure Chemical Industries, Ltd.) and mixed in an agate mortar toprepare a cobalt (II) chloride hexahydrate/PY 110 mixture (35A).

(2) Infusibilization and Carbonization

The mixture (35A) (1.031 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (35A) is heated at a rate of temperature rise of 10° C./min from30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled to roomtemperature over a period of 3 hours to obtain 0.540 g of a carbonmaterial (35B).

(3) Grinding and Acid Cleaning

The carbon material (35B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 110° C. for 1 hour to obtain an acidcleaned carbon material (35C).

Molecular formula: C₂₂H₆Cl₈N₄O₂Molecular weight: 641.933Elemental analysis (calcd.): C, 41.16; H, 0.94; Cl, 44.18; N, 8.73; O,4.98.

Example 36 Synthesis of Carbon Material (36C) from Cobalt (II) ChlorideHexahydrate/PY 139 Mixture (1) Preparation of Cobalt (II) ChlorideHexahydrate/PY 139 Mixture

To 4.00 g of Pigment Yellow 139 (PY 139) (Chromophtal Yellow 2RF, fromBASF Japan Ltd.) is added 0.864 g of cobalt (II) chloride hexahydrate(from Wako Pure Chemical Industries, Ltd.) and mixed in an agate mortarto prepare a cobalt (II) chloride hexahydrate/PY 139 mixture (36A).

(2) Infusibilization and Carbonization

The mixture (36A) (1.020 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (36A) is heated at a rate of temperature rise of 10° C./min from30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled to roomtemperature over a period of 3 hours to obtain 0.331 g of a carbonmaterial (36B).

(3) Grinding and Acid Cleaning

The carbon material (36B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 110° C. for 1 hour to obtain an acidcleaned carbon material (36C).

Molecular formula: C₁₆H₉N₅O₆Molecular weight: 367.273Elemental analysis (calcd.): C, 52.32, H, 2.47; N, 19.07; O, 26.14.

Example 28 Synthesis of Carbon Material (28C) from Cobalt (II) ChlorideHexahydrate/1,2,4,5-Tetracyanobenzene (TCB) Mixture (1) Preparation ofCobalt (II) Chloride Hexahydrate/TCB Mixture

To 5.27 g of 1,2,4,5-tetracyanobenzene (TCB) (from Tokyo ChemicalIndustry Co., Ltd.) is added 1.17 g of cobalt (II) chloride hexahydrate(from Wako Pure Chemical Industries, Ltd.) and mixed in an agate mortarto prepare a cobalt (II) chloride hexahydrate/TCB mixture (28A).

(2) Infusibilization and Carbonization

The mixture (28A) (1.008 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (28A) is heated at a rate of temperature rise of 5 C/min from30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled to roomtemperature over a period of 30 minutes to obtain 0.071 g of a carbonmaterial (28B).

(3) Grinding and Acid Cleaning

The carbon material (28B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (28C).

1,2,4,5-Tetracyanobenzene

Molecular formula: C₁₀H₂N₄Molecular weight: 178.15Elemental analysis (calcd.): C, 67.42; H, 1.13; N, 31.45.

Example 29 Synthesis of Carbon Material (29C) from Cobalt (II) ChlorideHexahydrate/3,4,5,6-Tetrachlorophthalonitrile (TCPN) Mixture (1)Preparation of Cobalt (II) Chloride Hexahydrate/TCPN Mixture

To 5.03 g of 3,4,5,6-tetrachlorophthalonitrile (TCPN) (from SigmaAldrich Corporation) is added 0.75 g of cobalt (II) chloride hexahydrate(from Wako Pure Chemical Industries, Ltd.) and mixed in an agate mortarto prepare a cobalt (II) chloride hexahydrate/TCPN mixture (29A).

(2) Infusibilization and Carbonization

The mixture (29A) (1.004 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (29A) is heated at a rate of temperature rise of 500° C./minfrom 30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled toroom temperature over a period of 30 minutes to obtain 0.040 g of acarbon material (29B).

(3) Grinding and Acid Cleaning

The carbon material (29B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (29C).

3,4,5,6-Tetrachlorophthalonitrile

Molecular formula: C₅N₂Cl₄Molecular weight: 265.91Elemental analysis (calcd.): C, 36.13; H, 0.00; N, 10.53; Cl, 53.33.

Example 30 Synthesis of Carbon Material (30C) from Cobalt (II) ChlorideHexahydrate/7,7,8,8-Tetracyanoquinodimethane (TCNQ) Mixture (1)Preparation of Cobalt (II) Chloride Hexahydrate/TCNQ Mixture

To 1.98 g of 7,7,8,8-tetracyanoquinodimethane (TCNQ) (from TokyoChemical Industry Co., Ltd.) is added 0.384 g of cobalt (II) chloridehexahydrate (from Wako Pure Chemical Industries, Ltd.) and mixed in anagate mortar to prepare a cobalt (II) chloride hexahydrate/TCNQ mixture(30A).

(2) Infusibilization and Carbonization

The mixture (30A) (1.004 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (30A) is heated at a rate of temperature rise of 5° C./min from30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled to roomtemperature over a period of 30 minutes to obtain 0.141 g of a carbonmaterial (30B).

(3) Grinding and Acid Cleaning

The carbon material (30B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (30C).

7,7,8,8-Tetracyanoquinodimethane

Molecular formula: C₁₂H₄N₄Molecular weight: 204.187Elemental analysis (calcd.): C, 70.59; H, 1.97; N, 27.44.

Example 31 Synthesis of Carbon Material (31C) from Cobalt (II) ChlorideHexahydrate/2,3-Dichloro-5,6-Dicyano-1,4-Benzoquinone (DDQ) Mixture (1)Preparation of Cobalt (II) Chloride Hexahydrate/DDQ Mixture

To 4.00 g of 2,3-dichloro-5,6-dicyano-1,4-benzoquinone (DDQ) (from WakoPure Chemical Industries, Ltd.) is added 0.699 g of cobalt (II) chloridehexahydrate (from Wako Pure Chemical Industries, Ltd.) and mixed in anagate mortar to prepare a cobalt (II) chloride hexahydrate/DDQ mixture(31A).

(2) Infusibilization and Carbonization

The mixture (31A) (1.052 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (31A) is heated at a rate of temperature rise of 5° C./min from30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled to roomtemperature over a period of 30 minutes to obtain 0.042 g of a carbonmaterial (31B).

(3) Grinding and Acid Cleaning

The carbon material (31B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (31C).

Molecular formula: C₈Cl₂N₂O₂Molecular weight: 227.004Elemental analysis (calcd.): C, 42.33; C, 31.24; N, 12.34; O, 14.10.

Example 32 Synthesis of Carbon Material (32C) from Cobalt (II) ChlorideHexahydrate/4,5-Dichlorophthalamide (DCPA) Mixture (1) Preparation ofCobalt (II) Chloride Hexahydrate/DCPA Mixture

To 5.00 g of 4,5-dichlorophthalamide (DCPA) (from Tokyo ChemicalIndustry Co., Ltd.) is added 0.85 g of cobalt (II) chloride hexahydrate(from Wako Pure Chemical Industries, Ltd.) and mixed in an agate mortarto prepare a cobalt (II) chloride hexahydrate/DCPA mixture (32A).

(2) Infusibilization and Carbonization

The mixture (32A) (1.014 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (32A) is heated at a rate of temperature rise of 5° C./min from30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled to roomtemperature over a period of 30 minutes to obtain 0.041 g of a carbonmaterial (32B).

(3) Grinding and Acid Cleaning

The carbon material (32B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (32C).

4,5-Dichlorophthalamide

Molecular formula: C₈H₆N₂O₂Cl₂Molecular weight: 233.05Elemental analysis (calcd.): C, 41.23; H, 2.59; N, 12.02; O, 13.73; Cl,30.42.

Example 33 Synthesis of Carbon Material (33C) from Cobalt (II) ChlorideHexahydrate/2,6-Dicyanopyridine (2,6-DCPy) Mixture (1) Preparation ofCobalt (II) Chloride Hexahydrate/2,6-DCPy Mixture

To 5.16 g of 2,6-dicyanopyridine (2,6-DCPy) (from Sigma AldrichCorporation) is added 1.58 g of cobalt (II) chloride hexahydrate (fromWako Pure Chemical Industries, Ltd.) and mixed in an agate mortar toprepare a cobalt (II) chloride hexahydrate/2,6-DCPy mixture (33A).

(2) Infusibilization and Carbonization

The mixture (33A) (1.027 g) is weighed into a quartz boat. The quartzboat is placed in the middle of a quartz tube (outer diameter: 4.0 cm;inner diameter: 3.6 cm) inserted in a tubular furnace. Nitrogen is madeto flow at a rate of 300 ml/min for 30 minutes at room temperature. Themixture (33A) is heated at a rate of temperature rise of 5° C./min from30° C. to 700° C., maintained at 700° C. for 1 hour, and cooled to roomtemperature over a period of 30 minutes to obtain 0.140 g of a carbonmaterial (33B).

(3) Grinding and Acid Cleaning

The carbon material (33B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (33C).

2,6-Dicyanopyridine

Molecular formula: C₇H₃N₃Molecular weight: 129.12Elemental analysis (calcd.): C, 65.11; H, 2.34; N, 32.54.

Comparative Example 4 Synthesis of Carbon Material (C4C) from CobaltPhthalocyanine (Co-Pc) (1) Infusibilization and Carbonization

Cobalt phthalocyanine (Co-Pc) (from Sigma Aldrich Corporation) (1.005 g)is weighed into a quartz boat. The quartz boat is placed in the middleof a quartz tube (outer diameter: 4.0 cm; inner diameter: 3.6 cm)inserted in a tubular furnace. Nitrogen is made to flow at a rate of 300ml/min for 30 minutes at room temperature. The Fe-Pc is heated at a rateof temperature rise of 1° C./min from 30° C. to 300° C. and then at 10°C./min from 300° C. to 700° C., maintained at 700° C. for 1 hour, andcooled to room temperature over a period of 3 hours to obtain 0.789 g ofa carbon material (C4B).

(2) Grinding and Acid Cleaning

The carbon material (C4B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (C4C).

Molecular formula: C₃₂H₁₆C0N₈Molecular weight: 571.456Elemental analysis (calcd.): C, 67.26; H, 2.82; Co, 10.31; N, 19.61.

Comparative Example 5 Synthesis of Carbon Material (C5C) from Co-PQ (1)Synthesis of Polyquinolinol (PQ)

In a 100 ml recovery flask are put 10 g of 8-quinolinol, 10 g offormaldehyde, and 1 g of oxalic acid dihydrate and refluxed at 100° C.overnight. To the mixture is added 5.5 ml of 1M HCl, followed byrefluxing under the same conditions overnight. The resulting solid iscollected by filtration by suction, washed three times with distilledwater, and dried in vacuo overnight to yield PQ.

(2) Preparation of Cobalt Polyquinolinol Complex (Co-PQ)

In 100 ml of N,N-dimethylformamide is dissolved 3.3 g of PQ, and asolution of 0.9 g of cobalt (II) chloride in 50 ml of dimethylacetamide(DMAc) is added thereto. After allowing the mixed solution to standstill overnight, the solution is concentrated using an evaporator (90°C.) and added dropwise to 3000 ml of water. The precipitate thus formedis collected by filtration, reprecipitated from DMAc, and collected byfiltration to obtain a cobalt polyquinolinol complex (Co-PQ). Thecomposition of Co-PQ is found to be Co(PQ)₃.

(3) Infusibilization and Carbonization

Co-PQ (1.001 g) is weighed into a quartz boat. The quartz boat is placedin the middle of a quartz tube (outer diameter: 4.0 cm; inner diameter:3.6 cm) inserted in a tubular furnace. Nitrogen is made to flow at arate of 300 ml/min for 30 minutes at room temperature. The Co-PQ isheated at a rate of temperature rise of 1° C./min from 30° C. to 300° C.and then at 10° C./min from 300° C. to 700° C., maintained at 700° C.for 1 hour, and cooled to room temperature over a period of 3 hours toobtain 0.522 g of a carbon material (C5B).

(4) Grinding and Acid Cleaning

The carbon material (C5B) is ground in an agate mortar. The powder iswashed with concentrated hydrochloride acid three times, each followedby filtration, washed with water, and air dried. The resulting carbonmaterial is dried in vacuo at 60° C. overnight to obtain an acid cleanedcarbon material (C5C).

Molecular formula: (C₁₀H₇NO)_(n)Molecular weight (Mw): 14,000Elemental analysis (calcd.): C, 76.42; H, 4.49; N, 8.91; O, 10.18.

Cobalt Polyquinolinol Complex (Co-PQ):

Molecular formula: (C₃₀H₂₁N₃O₃Co)_(n)Formula weight: 530.44Elemental analysis (calcd.): C, 67.9; H, 4.43; N, 7.92; O, 9.05; Co,11.10.

Comparative Example 6 Synthesis of Carbon Material (C6C) from Cobalt(II) Chloride Hexahydrate/Acetonitrile (MeCN) Mixture Preparation ofCobalt (II) Chloride Hexahydrate/MeCN Mixture, Infusibilization, andCarbonization

Acetonitrile (MeCN) (0.5 g) (from Wako Pure Chemical Industries, Ltd.)and 0.50 g of cobalt (II) chloride hexahydrate are weighed into a quartzboat. The quartz boat is placed in the middle of a quartz tube (outerdiameter: 4.0 cm; inner diameter: 3.6 cm) inserted in a tubular furnace.Nitrogen is made to flow at a rate of 300 ml/min for 30 minutes at roomtemperature. The cobalt (II) chloride hexahydrate/MeCN mixture is heatedat a rate of temperature rise of 10° C./min from 30° C. to 700° C.,maintained at 700° C. for 1 hour, and cooled to room temperature over aperiod of 3 hours. The resulting purple residue (C6B) is washed withconcentrated hydrochloride acid three times, each followed byfiltration, washed with water, and air dried. Nothing remained on thefilter paper, meaning a failure to obtain a carbon material.

Evaluation of Physical Properties of Organic Material:

Heat resistance of the organic materials used in Examples 1 to 33 andComparative Examples 3 to 5 is evaluated by determining a percent massloss (ΔTG) at 400° C. relative to the mass at room temperature in TG-DTAanalysis at a rate of temperature rise of 10° C./min from 30° C. to1000° C. in a nitrogen atmosphere. TG-DTA analysis is performed onEXSTAR 6000 series TG/DTA 6200 from SII Nanotechnology Corporation. Theresults obtained are shown in Tables 1 to 3.

Making Carbon Alloy-Coated Electrode:

Each of the carbon alloy materials obtained in Examples 1 to 33 andComparative Examples 1 to 6 weighing 10 mg is mixed with 110 mg of aNafion solution (5% alcoholic aqueous solution) as a binder, 2.4 ml ofwater and 1.6 ml of 1-propanol as solvents and dispersed in anultrasonic homogenizer (horn tip diameter: 7 mm) (from Nippon Seiki Co.,Ltd.) for 30 minutes. A 4 μl aliquot of the dispersion is applied to arotating disk electrode and dried at room temperature to make a carbonalloy-coated electrode. The characteristics of the resulting carbonalloy-coated electrode are evaluated as follows. The results obtainedare shown in Tables 1 to 3.

Determination of ORR Activity:

Automatic polarization system HZ-3000 (from Hokuto Denko Corp.) equippedwith a disk electrode rotator HR-201 (from Hokuto Denko) is used forlinear sweep voltammetry (LSV) according to the following procedures.The carbon alloy-coated electrode is set as a working electrode. Aplatinum electrode and a saturated calomel electrode (SCE) are used as acounter electrode and a reference electrode, respectively.

Procedures:

(a) The carbon alloy-coated electrode is cleaned by cyclic voltammetryin a 0.1M sulfuric acid aqueous solution at 20° C. through which argonhad been bubbled for at least 30 minutes at a sweep rate of 50 mV/s witha sweep potential ranging from 0.946 to −0.204 V (vs. SCE) for 10cycles.(b) To obtain blank data, LSV is carried out in a 0.1 M sulfuric acidaqueous solution at 20° C. through which argon had been bubbled for atleast 30 minutes at a sweep rate of 5 mV/s with a sweep potentialranging from 0.746 to −0.204 V (vs. SCE) and at an electrode rotationspeed of 1500 rpm.(c) For ORR activity determination, LSV is performed in a 0.5 M sulfuricacid aqueous solution through which oxygen had been bubbled for at least30 minutes at a sweep rate of 5 mV/s with a sweep potential ranging from0.746 to −0.204 V (vs. SCE) and at an electrode rotation speed of 1500rpm.(d) The blank data obtained in (b) above is subtracted from the data of(c) to obtain a true oxygen reduction current. The current density atthe voltage of 0.5 V (vs. NHE) is obtained from the resultingvoltammogram (voltage-current density curve, see FIG. 3), which is takenas an ORR activity value.

BET Specific Surface Area:

The sample is dried at 200° C. in vacuo for 3 hours using a pretreatmentinstrument BELPREP-flow (from Bel Japan, Inc.). The specific surfacearea measurement is performed using an automatic specific surfacearea/pore distribution measurement instrument BELSOPR-mini II (from BelJapan, Inc.) under simplified measuring conditions. Specific surfacearea analysis is carried out by the BET method using the attachedanalysis program.

Raman Microscopy:

A dispersive Raman system T6400 (from HORIBA Jobin Yvon Inc.) equippedwith an Ar ion laser (514.5 nm excitation) and a 100× power objective (1μm resolution) is used to obtain a Raman spectrum. The resulting Ramanspectrum is subjected to wave separation to be divided into D-band(C(sp3)) and G-band (C(sp2)) appearing at about 1320 cm⁻¹ and about 1600cm⁻¹, respectively. The full width at half maximum of the D-band (ΔD) isobtained, which is taken as a measure of turbostraticity.

TABLE 1 Organic Material Composition ΔTG at 400° C. ORR Activity A BETSpecific Turbostraticity A B C (%) (μA/cm²) Surface Area (m²/g) ΔD(cm⁻¹) Example 1 PR 254 −1 −100 232 138 Comp. Example 1 PhOH −100 — — —Comp. Example 2 MeCN −100 — — —

TABLE 2 Organic Material Composition ΔTG at 400° C. ORR Activity A BETSpecific Turbostraticity A B C (%) (μA/cm²) Surface Area (m²/g) ΔD(cm⁻¹) Example 2 PR 202 FeCl₃•6H₂O −25 −128 269 110  Example 3 PO 71FeCl₃•6H₂O −25 −151 312 — Example 4 PR 254 FeCl₃ −10 −131 166 80 Example5 PR 254 FeCl₃•6H₂O −27 −563 325 — Example 6 PR 254-LP FeCl₃•6H₂O −39−730 321 — Example 7 PR 254 FeCl₃•6H₂O −20 −250 374 83 Example 8 PR 254FeCl₂•4H₂O −8 −302 394 103  Example 9 DCP FeCl₃•6H₂O −56 −418 163 —Comp. Example 3 Fe-Pc −6 −70 137 58

TABLE 3 ΔTG at ORR BET Specific Turbo- Organic Material Composition 400°C. Activity A Surface straticity A B C (%) (μA/cm²) Area (m²/g) ΔD(cm⁻¹) Example 10 DCP CoCl₂•6H₂O −70 −2094 361  84 Example 11 PR 122CoCl₂•6H₂O −11  −105  91 101 Example 12 4-HPN CoCl₂•6H₂O −32  −119  89 —Example 13 4,5-DHBN CoCl₂•6H₂O −54  −244 244 — Example 14 PN CoCl₂•6H₂O−61 −1055 100 — Example 15 PN CoCl₂•6H₂O VB −45  −448 116 — Example 164-HPN CoCl₂•6H₂O VB −42  −795 132 — Example 17 MN CoCl₂•6H₂O −55  −774199 — Example 18 2-CBA CoCl₂•6H₂O −67  −789 229 — Example 19 3-CBACoCl₂•6H₂O −79  −766 108 — Example 20 Cl—Ph—CN CoCl₂•6H₂O −87  −500  29— Example 21 Cl—Ph—CN CoCl₂•6H₂O KB −42  −478 662 — Example 22 DCPCoCl₂•6H₂O VB −48  −680 112 — Example 23 PR 254-LP CoCl₂•6H₂O −41  −967387 — Example 24 PR 254 Co(NO₃)₂•6H₂O −23 −1022 376 127 Example 25 PR245 CoCl₂•6H₂O −10 −1067 319 145 Example 26 PY 138 CoCl₂•6H₂O  −7  −583180 — Example 27 PY 185 CoCl₂•6H₂O −26 −1122 484 — Example 34 PY 109CoCl₂•6H₂O  −6  −475  77 — Example 35 PY 110 CoCl₂•6H₂O  −6  −579 111 —Example 36 PY 139 CoCl₂•6H₂O −22 −1410 234 — Example 28 TCB CoCl₂•6H₂O−83 −1693  63 — Example 29 TCPN CoCl₂•6H₂O −90 −1369 238 — Example 30TCNQ CoCl₂•6H₂O −89 −1131  47 — Example 31 DDQ CoCl₂•6H₂O −92 −1359  86— Example 32 DCPA CoCl₂•6H₂O −85 −2060 308 — Example 33 2,6-DCPyCoCl₂•6H₂O −84 −1339 165 — Comp. Example 4 Co—Pc  −2  −35 134 — Comp.Example 5 C—PQ −20  −32 134  40 Comp. Example 6 MeCN CoCl₂•6H₂O — — — —

1. A nitrogen-containing carbon alloy obtained by baking an organicmaterial comprising a nitrogen-containing crystalline organic compoundhaving a molecular weight of 60 to 2000, wherein the nitrogen-containingcrystalline organic compound excludes a nitrogen-containing metalcomplex.
 2. The nitrogen-containing carbon alloy according to claim 1,wherein the organic material further comprises at least one of aninorganic metal and an inorganic metal salt.
 3. The nitrogen-containingcarbon alloy according to claim 1, wherein the nitrogen-containingcrystalline organic compound is a nitrile compound, an amide compound ora quinacridone compound.
 4. The nitrogen-containing carbon alloyaccording to claim 1, wherein the nitrogen-containing crystallineorganic compound has at least one group selected from the groupconsisting of a nitrile group, an amido group and 4-quinolone structure,and an unsaturated bond per molecule.
 5. The nitrogen-containing carbonalloy according to claim 4, wherein the nitrogen-containing crystallineorganic compound has at least one selected from the group consisting ofa nitrile group and an amido group, at least one selected from the groupconsisting of a nitrile group, an amido group, a halogen atom, and ahydroxyl group, and an unsaturated bond per molecule.
 6. Thenitrogen-containing carbon alloy according to claim 1, wherein thenitrogen-containing crystalline organic compound is a pigment.
 7. Thenitrogen-containing carbon alloy according to claim 1, wherein thenitrogen-containing crystalline organic compound has a nitrogen contentof 0.1% to 55% by mass.
 8. The nitrogen-containing carbon alloyaccording to claim 1, wherein the organic material is avolatile-retardant compound having a ΔTG value of −95% to −0.1% at 400°C. in a nitrogen atmosphere.
 9. The nitrogen-containing carbon alloyaccording to claim 1, wherein the baking is carried out at a bakingtemperature of 500° to 1000° C. in a stream of inert gas ornon-oxidizing gas.
 10. The nitrogen-containing carbon alloy according toclaim 9, wherein the inert gas or non-oxidizing gas flows at a flow rateof 0.01 to 2.0 l/min per 36 mm inner diameter.
 11. A process forproducing the nitrogen-containing carbon alloy according to claim 2,comprising: mixing the nitrogen-containing crystalline organic compoundand the at least one of the inorganic metal and the inorganic metalsalt; raising a temperature of the mixture from room temperature to acarbonization temperature of the mixture in an inert atmosphere at arate of 1° C./min to 1000° C./min; maintaining the mixture at atemperature of 500° to 1000° C. for 0.1 to 100 hours to achievecarbonization; and cooling the carbonized mixture from the carbonizationtemperature to room temperature.
 12. A carbon catalyst comprising thenitrogen-containing carbon alloy according to claim
 1. 13. A fuel cellcomprising the carbon catalyst according to claim 12 and apolyelectrolyte.
 14. An electrical storage device comprising the carboncatalyst according to claim 12.